JPH09103791A - Septic tank - Google Patents
Septic tankInfo
- Publication number
- JPH09103791A JPH09103791A JP26294895A JP26294895A JPH09103791A JP H09103791 A JPH09103791 A JP H09103791A JP 26294895 A JP26294895 A JP 26294895A JP 26294895 A JP26294895 A JP 26294895A JP H09103791 A JPH09103791 A JP H09103791A
- Authority
- JP
- Japan
- Prior art keywords
- membrane
- sewage
- water
- tank
- aeration
- 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
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
- Treatment Of Biological Wastes In General (AREA)
Abstract
Description
【0001】[0001]
【発明が属する技術分野】本発明は、液中膜体を用いて
雑排水、し尿を処理する浄化槽や、工場工程排水を処理
する産業用の浄化槽に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a septic tank for treating gray water and human waste by using a submerged membrane, and an industrial septic tank for treating factory process wastewater.
【0002】[0002]
【従来の技術】従来、液中膜体を用いて汚水を処理する
浄化槽が多用されている。この種の浄化槽に用いられる
液中膜体は、汚水中の比較的大きな分子の透過を膜面で
阻止する一方、比較的小さな分子である水を透過させる
微孔を有している。これらの液中膜体は例えば曝気用の
散気管上部に設置され、曝気攪拌の水流と気泡が膜体の
表面に接触し、膜面を振動させながら上昇することによ
り、この膜面に付着した汚水物質を洗浄し、汚水物質に
よる目詰まりを抑制するようになっている。2. Description of the Related Art Conventionally, a septic tank for treating sewage using a submerged membrane has been widely used. The submerged membrane used in this type of septic tank has micropores that prevent the permeation of relatively large molecules in wastewater on the membrane surface, while allowing the permeation of relatively small molecules of water. These submerged membranes are installed, for example, in the upper part of the aeration pipe for aeration, and the aeration and agitation water flow and bubbles come into contact with the surface of the membrane and ascend while vibrating the membrane surface to adhere to this membrane surface. The sewage substance is washed to prevent clogging due to the sewage substance.
【0003】[0003]
【発明が解決しようとする課題】上記液中膜体は、曝気
攪拌の水流と気泡による洗浄手段で目詰まりを起こさな
いように一般に曝気用の散気管上部に設置されている
が、必ずしも十分な洗浄ができないため、目詰まりを起
こして、処理能力を低下させることがある。そこで本発
明では、液中膜体の膜面が汚水物質により目詰まりを起
こすことを確実に防止する浄化槽を提供することを解決
すべき課題とするものである。The above-mentioned submerged film body is generally installed on the upper part of the aeration pipe for aeration so as not to cause clogging by the cleaning means by the water flow and bubbles of aeration stirring, but it is not always sufficient. Since it cannot be washed, it may cause clogging and reduce the processing capacity. Therefore, it is an object of the present invention to provide a septic tank that reliably prevents the membrane surface of the submerged membrane from being clogged with a wastewater substance.
【0004】[0004]
【課題を解決するための手段】上記の課題を解決するた
めの第1の手段は、汚水を浄化する行程で用いられる液
中膜体に付着した汚水物質を超音波発振により発生した
キャビテ−ションでクリ−ニングするように浄化槽を構
成することである。A first means for solving the above problems is a cavitation generated by ultrasonic oscillation of a wastewater substance attached to a submerged membrane used in the process of purifying wastewater. Is to configure the septic tank so that it is cleaned.
【0005】上記構成の浄化槽によれば、超音波の発振
によるキャビテ−ションで液中膜体の膜面に付着した汚
水物質をクリ−ニングすることができ、液中膜体の目詰
まりを防止することができる。According to the septic tank having the above-mentioned structure, the sewage substance adhering to the film surface of the submerged membrane can be cleaned by the cavitation caused by the oscillation of ultrasonic waves, and the clogging of the submerged membrane can be prevented. can do.
【0006】また、課題を解決するための第2の手段
は、汚水の水分子を内部に透過させ、その水分子を処理
水として外部に放出する一方、水分子より大きな所定の
大きさを越える分子の汚水物質を透過させないように構
成した液中膜体下方からの散気による曝気攪拌の水流と
気泡の上昇力、及び超音波発振により発生したキャビテ
−ションにより、液中膜体に付着した汚水物質をクリ−
ニングするように浄化槽を構成することである。A second means for solving the problem is to allow water molecules of sewage to permeate into the inside and release the water molecules to the outside as treated water, while exceeding a predetermined size larger than the water molecules. Adhered to the submerged membrane body by the cavitation generated by the water flow and bubble rising force of aeration and stirring by aeration from the bottom of the submerged membrane body configured so as not to pass the filthy substance of the molecule, and the cavitation generated by ultrasonic oscillation Clear sewage substances
To configure the septic tank.
【0007】上記構成の浄化槽によれば、液中膜体下方
からの散気による曝気攪拌の水流と気泡の上昇力と、超
音波発振によるキャビテ−ションによる洗浄力との相乗
作用により液中膜体に付着した汚水物質が洗浄される。According to the septic tank having the above structure, the submerged membrane is synergized by the water flow of aeration and agitation due to air diffusion from below the submerged membrane and the ascending force of the bubbles, and the cleaning force by cavitation by ultrasonic oscillation. Sewage substances on the body are washed away.
【0008】[0008]
【発明の実施の形態】次に、本発明の実施の形態を図面
を参照しながら説明する。図1は、トイレ排水、洗濯排
水、炊事排水、浴室排水などの汚水を処理する合併式浄
化槽の処理行程を示した行程図である。尚、以下に説明
するそれぞれの槽は一般的なものであるため、各槽の作
用については説明しない。外部から流入したトイレ排
水、洗濯排水、炊事排水、浴室排水などの汚水は荒目ス
クリ−ン1を通り、曝気沈砂槽2に収容されて曝気され
る。沈砂された汚水は曝気沈砂槽2から原水ポンプ槽3
に流れて一時貯水されたあと、ポンプ4により流量調整
槽5に送水される。Next, embodiments of the present invention will be described with reference to the drawings. FIG. 1 is a process diagram showing a treatment process of a combined septic tank for treating wastewater such as toilet drainage, laundry drainage, cooking drainage, bathroom drainage and the like. Since each tank described below is a general one, the operation of each tank will not be described. Wastewater such as toilet drainage, laundry drainage, cooking drainage, bathroom drainage, etc. that has flowed in from the outside passes through the coarse screen 1 and is stored in the aeration sand settling tank 2 and aerated. The sewage that has been set aside is aerated and settling tank 2 to raw water pump tank 3
After being stored in the flow control tank 5, the water is temporarily stored and then sent to the flow rate adjusting tank 5 by the pump 4.
【0009】上記流量調整槽5に流入された汚水は、ブ
ロワ6から送られた空気を散気管7で散気させ、曝気さ
れる。この曝気された汚水はポンプ8により吸引され、
微細目スクリ−ン9を通過する過程で汚水中の比較的大
きな粒子がこの微細目スクリ−ン9により捕捉される。
この微細目スクリ−ン9を通過した汚水は、脱窒素槽1
0に流入され、窒素成分が除去される。そして窒素成分
が除去された汚水はポンプ11により硝化槽12に送水
される。尚、脱窒素槽10と硝化槽12の間には管13
が接続されており、硝化槽12の汚水が脱窒素槽10に
戻るように配管されている。The dirty water flowing into the flow rate adjusting tank 5 is aerated by diffusing the air sent from the blower 6 through the diffusing pipe 7. This aerated sewage is sucked by the pump 8,
In the process of passing through the fine screen 9, the relatively large particles in the wastewater are captured by the fine screen 9.
The wastewater that has passed through the fine screen 9 is denitrified tank 1
0, and nitrogen components are removed. Then, the wastewater from which the nitrogen component has been removed is sent to the nitrification tank 12 by the pump 11. A pipe 13 is provided between the denitrification tank 10 and the nitrification tank 12.
Are connected so that the wastewater in the nitrification tank 12 returns to the denitrification tank 10.
【0010】上記硝化槽12には、図2に示すような膜
体ユニット14が装備されている。この膜体ユニット1
4は、外枠板15内に着脱可能に取り付けられた複数の
膜カ−トリッジ16から成る。そしてこの膜体ユニット
14は、図1に示すようにブロワ17から送られた空気
を散気する散気管18の上部に取り付けられている。脱
窒素槽10から硝化槽12に送水された汚水は、この散
気管18からの散気による曝気攪拌の水流と気泡ととも
に、それぞれの膜カ−トリッジ16の膜表面に接触しな
がら上昇する。The nitrification tank 12 is equipped with a membrane unit 14 as shown in FIG. This membrane unit 1
Reference numeral 4 is composed of a plurality of film cartridges 16 which are detachably mounted in the outer frame plate 15. The membrane unit 14 is attached to the upper part of an air diffuser 18 which diffuses the air sent from the blower 17, as shown in FIG. The sewage sent from the denitrification tank 10 to the nitrification tank 12 rises while contacting the membrane surface of each membrane cartridge 16 together with the aeration and agitation water flow and bubbles due to the diffusion from the diffusion pipe 18.
【0011】硝化槽12の汚水は、それぞれの膜カ−ト
リッジ16の膜表面に接触しながら上昇する際、水の分
子は膜体の微孔を通過する一方、浮遊物質や、硝化菌、
脱窒菌などは分子サイズが大きいため、膜体の微孔を通
過することはできない。これらの分子サイズの大きな物
質は、図示していない汚泥貯留槽に溜められる一方、そ
れぞれの膜カ−トリッジ16の膜体の微孔を透過して各
膜カ−トリッジ16の内部に浸入した水は、吸引ポンプ
19に接続されたパイプ20を通して消毒槽21に送水
される。消毒槽21に送られた上記処理水は、消毒槽2
1において消毒されたあと処理水槽22に貯水され、ポ
ンプ23により外部に放流される。When the wastewater in the nitrification tank 12 rises while coming into contact with the membrane surface of each membrane cartridge 16, while the water molecules pass through the fine pores of the membrane body, floating substances, nitrifying bacteria,
Since denitrifying bacteria have a large molecular size, they cannot pass through the micropores of the membrane. While these substances having a large molecular size are stored in a sludge storage tank (not shown), the water that has penetrated into the inside of each membrane cartridge 16 through the fine pores of the membrane of each membrane cartridge 16 is infiltrated. Is sent to the disinfection tank 21 through the pipe 20 connected to the suction pump 19. The treated water sent to the disinfection tank 21 is used as the disinfection tank 2
After being sterilized in 1, the water is stored in the treated water tank 22 and discharged to the outside by the pump 23.
【0012】尚、図3は、汚水がそれぞれの膜カ−トリ
ッジ16の膜表面に接触しながら上昇する際、水の分子
Aは膜体16A,16Bの微孔を透過する一方、浮遊物
質や、硝化菌、脱窒菌などの分子サイズが大きい汚水物
質Bは膜体16A,16Bの微孔を通過しないように処
理される状況を示したものであり、Cは気泡、及び後述
の超音波発生器30の超音波発振によるキャビテ−ショ
ンを示している。図3に示すように、各膜カ−トリッジ
16は膜体16A,16Bの間に支持板16Cが設けら
れており、膜体16A,16Bの微孔を透過した水の分
子は、支持板16Cと膜体16A、及び支持板16Cと
膜体16Bの間の隙間に浸入する。そしてこの隙間に浸
入した水は前記パイプ20を通り、消毒槽21に送水さ
れる。In FIG. 3, when the sewage rises while coming into contact with the membrane surface of each membrane cartridge 16, the water molecule A permeates through the fine pores of the membrane bodies 16A and 16B, while floating substances and , A nitrifying bacterium, a denitrifying bacterium, and the like have a large molecular size, and a wastewater substance B is treated so as not to pass through the fine pores of the membrane bodies 16A and 16B. The cavitation by the ultrasonic oscillation of the container 30 is shown. As shown in FIG. 3, each film cartridge 16 is provided with a support plate 16C between the film bodies 16A and 16B, and the molecules of water which have permeated through the micropores of the film bodies 16A and 16B are supported by the support plate 16C. And the film body 16A and the gap between the support plate 16C and the film body 16B. The water that has entered this gap passes through the pipe 20 and is sent to the disinfection tank 21.
【0013】以上のように構成された浄化槽において、
膜体ユニット14のそれぞれの膜カ−トリッジ16の膜
表面には前述の浮遊物質や、硝化菌、脱窒菌などの分子
サイズの大きな物質が付着しやすい。そのため、前述の
散気管18からの散気による曝気攪拌の水流と気泡の上
昇力、及び、図2に示すように、散気管18の下部に超
音波発生器30を配設することにより、超音波発生器3
0から超音波を発振させ、この超音波発振によるキャビ
テ−ションの破裂現象の相乗作用により、それぞれの膜
カ−トリッジ16の膜表面に付着した上記汚水物質が十
分にクリ−ニングされる。In the septic tank constructed as described above,
The above-mentioned floating substances and substances having a large molecular size such as nitrifying bacteria and denitrifying bacteria are likely to adhere to the film surface of each film cartridge 16 of the film unit 14. Therefore, the water flow of aeration and agitation due to air diffusion from the air diffuser 18 and the ascending force of the bubbles, and as shown in FIG. Sound wave generator 3
An ultrasonic wave is oscillated from 0, and the sewage substance adhering to the film surface of each film cartridge 16 is sufficiently cleaned by the synergistic effect of the cavitation rupture phenomenon due to the ultrasonic wave oscillation.
【0014】図4は超音波発生器30の平面図であり、
図5はその一部破断正面図である。図4、図5におい
て、超音波発生器30の上面に明けられたそれぞれの孔
30Aには超音波振動子31が取り付けられている。そ
して、各超音波振動子31に接続されるケ−ブルはエル
ボ32から入線される。この超音波発生器30は水密に
構成されており、内部に水が浸入しないようになってい
るため、この超音波発生器30を図2に示すように液中
に浸漬させることができる。FIG. 4 is a plan view of the ultrasonic wave generator 30.
FIG. 5 is a partially cutaway front view thereof. 4 and 5, an ultrasonic transducer 31 is attached to each hole 30A formed in the upper surface of the ultrasonic generator 30. Then, the cable connected to each ultrasonic transducer 31 is inserted from the elbow 32. The ultrasonic wave generator 30 is watertight so that water does not enter the inside. Therefore, the ultrasonic wave generator 30 can be immersed in a liquid as shown in FIG.
【0015】以上の実施の形態では、硝化槽12に配設
された膜体ユニット14を対象にして超音波発生器30
を設けた例を示したが、この膜体ユニット14に限ら
ず、液中半透過膜を使用している箇所に超音波発生器を
使用することにより、膜表面に付着した汚水物質をクリ
−ニングすることができる。また、以上の実施の形態で
は、合併式浄化槽の例を示したが、合併式浄化槽に限ら
ずに通常用いられる浄化槽、産業用の浄化槽、あるいは
透過膜分離法でも本実施の形態の範疇に入る。In the above embodiment, the ultrasonic generator 30 is targeted for the membrane unit 14 disposed in the nitrification tank 12.
Although an example in which the above is provided, an ultrasonic generator is used not only in the membrane unit 14 but also in a place where a semipermeable membrane in liquid is used, so that the wastewater substance attached to the membrane surface can be removed. Can be trained. Further, in the above embodiment, an example of the combined septic tank is shown, but not limited to the combined septic tank, a septic tank that is normally used, an industrial septic tank, or a permeable membrane separation method is also included in the scope of this embodiment. .
【0016】[0016]
【発明の効果】以上のように第1の発明によれば、雑排
水や、し尿を処理する行程で用いられる液中膜体に付着
した汚水成分を超音波により発生したキャビテ−ション
でクリ−ニングすることができるため、膜体の目詰まり
を防止し、汚水処理の能力が低下することを防止する効
果がある。As described above, according to the first aspect of the present invention, the sewage component adhered to the submerged membrane used in the process of treating gray water and human waste is cleared by cavitation generated by ultrasonic waves. Therefore, it is possible to prevent clogging of the membrane body and prevent deterioration of sewage treatment ability.
【0017】また、第2の発明によれば、雑排水や、し
尿を処理する行程で用いられる液中膜体に付着した汚水
成分を、液中膜体下方からの散気による曝気攪拌の水流
と気泡の上昇力、及び、超音波発振によるキャビテ−シ
ョンによる洗浄力との相乗作用によりクリ−ニングする
ことができるため、膜体の目詰まりを防止し、汚水処理
の能力が低下することを防止する効果がある。Further, according to the second aspect of the present invention, the sewage component adhered to the submerged membrane used in the process of treating gray water and human waste is aerated by aeration from below the submerged membrane. Since cleaning can be performed by the synergistic effect of the ascending force of air bubbles and bubbles and the cleaning force of cavitation due to ultrasonic oscillation, it is possible to prevent clogging of the membrane and reduce the wastewater treatment ability. It has the effect of preventing.
【図1】浄化槽の全体的な処理行程を示した行程図であ
る。FIG. 1 is a process diagram showing an overall processing process of a septic tank.
【図2】膜体ユニットに対する超音波発生器の配置を示
した斜視図である。FIG. 2 is a perspective view showing an arrangement of ultrasonic generators with respect to a membrane unit.
【図3】膜カ−トリッジの作用説明図である。FIG. 3 is an explanatory view of the action of a film cartridge.
【図4】超音波発生器の平面図である。FIG. 4 is a plan view of an ultrasonic wave generator.
【図5】超音波発生器の正面図である。FIG. 5 is a front view of an ultrasonic wave generator.
2 曝気沈砂槽 3 原水ポンプ槽 5 流量調整槽 10 脱窒素槽 12 硝化槽 14 膜体ユニット 16 膜カ−トリッジ 19 吸引ポンプ 21 消毒槽 22 処理水槽 30 超音波発生器 31 超音波振動子 2 Aeration sedimentation tank 3 Raw water pump tank 5 Flow rate adjustment tank 10 Denitrification tank 12 Nitrification tank 14 Membrane unit 16 Membrane cartridge 19 Suction pump 21 Disinfection tank 22 Treatment water tank 30 Ultrasonic generator 31 Ultrasonic transducer
Claims (2)
体に付着した汚水物質を超音波発振により発生したキャ
ビテ−ションでクリ−ニングすることを特徴とする浄化
槽。1. A septic tank characterized by cleaning sewage substances adhering to a submerged membrane used in the step of purifying sewage with cavitation generated by ultrasonic oscillation.
分子を処理水として外部に放出する一方、水分子より大
きな所定の大きさを越える分子の汚水物質を透過させな
いように構成した液中膜体下方からの散気による曝気攪
拌の水流と気泡の上昇力、及び超音波発振により発生し
たキャビテ−ションにより、液中膜体に付着した汚水物
質をクリ−ニングすることを特徴とする浄化槽。2. A liquid configured to allow water molecules of sewage water to permeate inside and release the water molecules to the outside as treated water, while preventing permeation of a waste water substance having a molecule larger than a predetermined size larger than the water molecule. It is characterized by cleaning the sewage substance adhering to the submerged membrane by the water flow of aeration and stirring by aeration from below the membrane, the rising force of the bubbles, and the cavitation generated by ultrasonic oscillation. Septic tank.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP26294895A JPH09103791A (en) | 1995-10-11 | 1995-10-11 | Septic tank |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP26294895A JPH09103791A (en) | 1995-10-11 | 1995-10-11 | Septic tank |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH09103791A true JPH09103791A (en) | 1997-04-22 |
Family
ID=17382786
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP26294895A Pending JPH09103791A (en) | 1995-10-11 | 1995-10-11 | Septic tank |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH09103791A (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20010037551A (en) * | 1999-10-18 | 2001-05-15 | 지영호 | Ultrasonic wave method and its device for waste water treatment using hollow fiber filter |
WO2010073442A1 (en) * | 2008-12-25 | 2010-07-01 | 志摩環境事業協業組合 | Immersion-type membrane separation apparatus |
JP2011189327A (en) * | 2010-03-17 | 2011-09-29 | Shima Kankyo Jigyo Kyogyo Kumiai | Flat plate-like membrane element and immersion type membrane separator using this element |
JP2014057965A (en) * | 2013-12-28 | 2014-04-03 | Shima Kankyo Jigyo Kyogyo Kumiai | Plate membrane element and immersing type membrane separator using the same |
JP2014057966A (en) * | 2013-12-28 | 2014-04-03 | Shima Kankyo Jigyo Kyogyo Kumiai | Plate membrane element and immersing type membrane separator using the same |
JP2014205110A (en) * | 2013-04-12 | 2014-10-30 | 国立大学法人三重大学 | Waste water treatment apparatus provided with solid-liquid separation unit |
WO2023132146A1 (en) * | 2022-01-06 | 2023-07-13 | 株式会社デンソー | Water treatment device |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01258707A (en) * | 1988-04-07 | 1989-10-16 | Mitsubishi Heavy Ind Ltd | Membrane separator |
JPH04363196A (en) * | 1991-06-06 | 1992-12-16 | Kubota Corp | Sewage treating device |
JPH054030A (en) * | 1991-06-27 | 1993-01-14 | Kubota Corp | Solid-liquid separator |
JPH05138164A (en) * | 1991-11-15 | 1993-06-01 | Tdk Corp | Water purifier |
JPH0563633B2 (en) * | 1986-07-23 | 1993-09-10 | Ulvac Corp |
-
1995
- 1995-10-11 JP JP26294895A patent/JPH09103791A/en active Pending
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0563633B2 (en) * | 1986-07-23 | 1993-09-10 | Ulvac Corp | |
JPH01258707A (en) * | 1988-04-07 | 1989-10-16 | Mitsubishi Heavy Ind Ltd | Membrane separator |
JPH04363196A (en) * | 1991-06-06 | 1992-12-16 | Kubota Corp | Sewage treating device |
JPH054030A (en) * | 1991-06-27 | 1993-01-14 | Kubota Corp | Solid-liquid separator |
JPH05138164A (en) * | 1991-11-15 | 1993-06-01 | Tdk Corp | Water purifier |
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KR20010037551A (en) * | 1999-10-18 | 2001-05-15 | 지영호 | Ultrasonic wave method and its device for waste water treatment using hollow fiber filter |
WO2010073442A1 (en) * | 2008-12-25 | 2010-07-01 | 志摩環境事業協業組合 | Immersion-type membrane separation apparatus |
JP2010149064A (en) * | 2008-12-25 | 2010-07-08 | Shima Kankyo Jigyo Kyogyo Kumiai | Immersion type membrane separation apparatus |
US9073012B2 (en) | 2008-12-25 | 2015-07-07 | Shimakankyoujigyou Kyougyoukumiai | Immersion-type membrane separation apparatus |
JP2011189327A (en) * | 2010-03-17 | 2011-09-29 | Shima Kankyo Jigyo Kyogyo Kumiai | Flat plate-like membrane element and immersion type membrane separator using this element |
JP2014205110A (en) * | 2013-04-12 | 2014-10-30 | 国立大学法人三重大学 | Waste water treatment apparatus provided with solid-liquid separation unit |
JP2014057965A (en) * | 2013-12-28 | 2014-04-03 | Shima Kankyo Jigyo Kyogyo Kumiai | Plate membrane element and immersing type membrane separator using the same |
JP2014057966A (en) * | 2013-12-28 | 2014-04-03 | Shima Kankyo Jigyo Kyogyo Kumiai | Plate membrane element and immersing type membrane separator using the same |
WO2023132146A1 (en) * | 2022-01-06 | 2023-07-13 | 株式会社デンソー | Water treatment device |
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