JP3688146B2 - Septic tank - Google Patents

Septic tank Download PDF

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Publication number
JP3688146B2
JP3688146B2 JP09878399A JP9878399A JP3688146B2 JP 3688146 B2 JP3688146 B2 JP 3688146B2 JP 09878399 A JP09878399 A JP 09878399A JP 9878399 A JP9878399 A JP 9878399A JP 3688146 B2 JP3688146 B2 JP 3688146B2
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Japan
Prior art keywords
water
tank
treated
membrane
upstream
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JP2000288564A (en
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八郎 佐藤
和之 本田
久人 辻川
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Kubota Corp
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Kubota Corp
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Description

【0001】
【発明の属する技術分野】
本発明は、被処理水を吸引して濾過膜を透過させる膜分離槽を備え、前記膜分離槽に供給される被処理水をあらかじめ生物処理する上流側槽を備え、濾過膜を透過した膜透過処理水を給水部に供給可能にする給水機構を備え、前記給水部に供給する前記膜透過処理水を消毒する消毒機構を設けてある浄化槽に関する。
【0002】
【従来の技術】
従来、この種の浄化槽としては、前記浄化槽に流入した被処理水が、そのまま、前記上流側槽に受け入れられ、しかも、全量を、前記濾過膜を通過させ、給水部に供給可能とする構成となっているものが提案されていた。
【0003】
【発明が解決しようとする課題】
しかし、前記浄化槽に流入する被処理水は、前記上流側槽であらかじめ生物処理されているべきものであるとは限らず、風呂排水等の低負荷の被処理水(以下低負荷被処理水と称する)のように、単に、浄化槽内の容積を圧迫するだけのものであって、前記浄水設備内の被処理水の処理を遅らせるものとなっている場合がある。ここで、前記被処理水の流入が連続したような場合に、槽内の水位が上がりすぎて、前記膜濾過の処理能力を超える場合がある。また、このような大量の被処理水の流入を受けると、前記上流側槽の被処理水が酸素富化状態になって、予備的な生物処理に悪影響を及ぼしやすいことと、このように大量流入した被処理水は、前記上流側槽の沈殿汚泥等を押し流し、前記膜分離槽に流入させてしまい、その膜分離槽にも悪影響を及ぼす可能性がある。
【0004】
また、膜濾過処理水の需要のある時間帯は一日の中で一部の時間帯に限られる場合が多く、低負荷被処理水が需要のない時間帯に大量流入したときに、未処理放流せざるを得なくなったりして有効利用がはかれない場合があった。
【0005】
従って、本発明の目的は、上記実状に鑑み、被処理水の大量流入を受けても、水処理環境に悪影響を与えにくく、かつ、膜透過処理水も有効利用できる浄化槽を提供することにある。
【0006】
【課題を解決するための手段】
この目的を達成するための本発明の浄化槽の第1特徴構成は、被処理水をあらかじめ生物処理する上流側槽と、生物処理された前記被処理水を吸引して濾過膜を透過させる膜分離槽と、前記濾過膜を透過した膜透過処理水を消毒する消毒槽と、消毒された前記膜透過処理水を給水部に供給可能にする給水機構とを設けてある浄化槽であって、前記消毒槽を前記上流側槽及び前記膜分離槽とは別槽に設け、前記上流側槽における原水流入側に、内部に濾材を配して下端部に開口部のある移流管を設け、前記移流管の上端部に、前記上流側槽を所定水位以上にする前記被処理水を前記膜分離槽を介さずに前記消毒槽に供給する越流機構を連通接続している点にある。
本発明の浄化槽の第2特徴構成は、被処理水を吸引して濾過膜を透過させる膜分離槽を備え、前記膜分離槽に供給される被処理水をあらかじめ生物処理する上流側槽を備え、濾過膜を透過した膜透過処理水を給水部に供給可能にする給水機構を備え、前記給水部に供給する前記膜透過処理水を消毒する消毒機構を設けてある浄化槽であって、前記上流側槽を所定水位以上にする被処理水を一時貯留可能にする貯留機構、及び、前記上流側槽を所定水位以上にする被処理水を前記膜分離槽を介さずに前記消毒機構に供給可能にする越流機構を設け、前記被処理水を前記貯留機構もしくは前記越流機構に択一的に供給切り替えする切り替え機構を設けている点にある。
【0007】
〔作用効果〕
つまり、被処理水を吸引して濾過膜を透過させる膜分離槽を備えた浄化槽は、その濾過膜を通過した膜透過処理水が粒子成分をほとんど含まず清浄なものとなっていることから、前記膜透過処理水を再利用に供することができるものとなっている。ここで、通常前記浄化槽は、前記膜分離槽に供給される被処理水をあらかじめ生物処理する上流側槽を備えているから、前記膜分離槽の負荷を安定させ、被処理水成分を長期的に安定した膜分離処理を可能にする。そのため、濾過膜を透過した膜透過処理水を給水部に供給可能にする給水機構を備えてあれば、清浄になった膜透過処理水を再利用することができる。この際、前記給水部に供給する前記膜透過処理水を消毒する消毒機構を設けてあれば、その再利用される膜透過処理水が、周辺環境に悪影響を与えないようにできる。
【0008】
ここで、前記膜透過処理水を安定供給するには、前記槽内の水処理と、被処理水供給とが安定している必要がある。そこで、大量に流入した被処理水は、前記越流機構により、前記上流側槽を所定水位以上にする被処理水を前記膜分離槽を介さずに前記消毒機構に供給することによって、たとえば、消毒のみで再利用可能にできる低負荷被処理水を給水部に供給することができるようになる。これにより、前記上流側槽は、所定水位以上にはならず、浄化槽全体としても安定した水処理能力を維持できるとともに、地上高位に供給される膜透過処理水を容易に得られる。
【0010】
さらに、前記上流側槽を所定水位以上にする被処理水を一時貯留可能にする貯留機構、及び、前記上流側槽を所定水位以上にする被処理水を前記膜分離槽を介さずに前記消毒機構に供給す可能にする越流機構を設け、前記被処理水を前記貯留機構もしくは前記越流機構に択一的に供給切り替えする切り替え機構を設けてあれば、たとえば、前記膜濾過被処理水を給水部に供給しているときに低負荷被処理水の流入を受けるおそれがあるような場合に、前記低負荷被処理水の供給先を前記貯留機構とし、それ以外の場合、あるいは、前記貯留機構が容量限界に達する場合に前記低負荷被処理水の供給先を前記越流機構とすることによって、確実に再生水を給水部に安定給水でき、かつ、安定した水処理が実現できる。
【0011】
【発明の実施の形態】
以下に本発明の実施の形態を図面に基づいて説明する。
図1に示す浄化設備は、本願独特の構成の浄化槽100と、これに接続される揚水配管101及び給水部102から構成されている。ここで、図1においては、給水部102が、屋根への散水部(散水設備)として構成されている例が示されている。
さて、浄化槽100について説明すると、これは、被処理水が上流側から夾雑物除去槽N、流量調整槽B1、沈殿汚泥貯留槽B2、膜分離槽Eを記載順に移流するように構成されており、各槽間は隔壁Wで仕切られている。ここで、前記夾雑物除去槽N、流量調整槽B1、沈殿汚泥貯留槽B2が、前記膜分離槽Eに対する上流側槽に該当する。
【0012】
前記夾雑物除去槽Nは、流入口Iから流入した原水を被処理水として受け、その被処理水から沈殿する固形物および液面に発生するスカム等の固体成分を分離しつつ、主に前記原水の液体成分を流量調整槽B1へ自然移流自在に構成し、内部には被処理水を嫌気分解する嫌気性菌を育成してある。
尚、図中Fは、夾雑物除去槽Nの幅方向中央部に開口部F1を設けた移流管であり、前記夾雑物除去槽Nの基準水位以上になった被処理水が濾材F2により濾過されて前記開口部から前記流量調整槽B1に流入するように構成したものである。また、前記移流管Fの上部には前記基準水位よりもやや上方の所定水位に達した被処理水を前記流量調整槽B1以外へ案内する第一、第二案内路G1,G2を設けてある。
【0013】
前記流量調整槽B1は、計量装置1aおよび移送用エアリフトポンプ1bを備えてなり、前記夾雑物除去槽Nから自然移流してきた被処理水の前記液体成分を一時貯留して、前記膜分離槽Eへ移送管1cを介してほぼ定量的に移送可能に形成してある。
【0014】
前記膜分離槽Eは、被処理水を複数の濾過膜としての平膜Mにより濾過して浄化するものであり、この膜分離槽E内では被処理水の有機成分を好気分解する好気性菌が育成されている。さらに、槽内に平膜Mを取り付けた状態で、その平膜Mの下方に、気泡を供給して、平膜M表面に汚泥等が付着するのを防止する散気管Dを設けてある。従って、この散気管Dより、散気操作することで前記好気性菌に酸素を供給し、かつ、前記平膜の表面を洗浄して、平膜Mの膜分離処理性能を高く維持できる。
【0015】
濾過膜としての前記平膜Mは、被処理水導通部を内方に有するABS樹脂製の支持板の両表面にポリエチレン製の濾過膜部材を接着形成するとともに、前記被処理水導通部に連通するノズル4を連設してなり、前記平膜Mを被処理水に浸漬した状態で、前記ノズル4から吸引操作すると、被処理水が前記濾過膜部材を通過して、その濾過膜部材によって被処理水中の汚泥等が除去され、高度に浄水された被処理水を取り出すことが出来る。ここで、この濾過膜部材6は、孔径0.4μm以下の精密濾過膜であり、このような孔径のものを選択することにより、長期間の使用に対して、膜内汚染を防止でき、長期メンテナンスフリーの運転が可能となる。
【0016】
前記ノズル4は、吸引ポンプ9に連通接続され、この吸引ポンプ9を運転操作する事で前記平膜Mで膜分離処理された被処理水(膜透過処理水と称する)を、浄化槽外部に設けられる消毒機構としての消毒槽Qへ送りだすとともに給水部に給水する給水機構として働く。ここで、図示するように、前記吸引ポンプ9は浄化槽側壁103外部部位に設けられてメンテナンスの容易性が確保されるとともに、吸引ポンプ9は、膜分離槽Eの最低水位より低い位置に配設されている。従って、吸引ポンプ9が停止した場合においても、吸引ポンプ9内には、被処理水が残留して、再始動時の呼び水となる。
【0017】
前記移流管F上部に設けた第一案内路G1は、前記消毒槽Qに連通接続されており、被処理水を前記膜分離槽Eを介さずに前記消毒槽Qに供給可能にする越流機構を構成している。前記夾雑物除去槽N及び流量調整槽B1の水位が高い場合に槽内に大量流入した低負荷被処理水をそのまま前記消毒槽Qに移送して、再生水として用いることができるようになっている。また、前記第二案内路G2は、前記浄化槽100の体とは別体に設けた一時貯留槽Tに連通接続してあり、先と同様の場合でも、昼間に前記低負荷処理水が大量流入して、前記用水配管からの給水と合流する可能性があるような場合には、前記第一案内路G1を閉鎖しておき、前記低負荷被処理水を一時貯留槽Tに貯留することができるように構成してある。尚、このような第一、第二案内路G1,G2の切り替えは、タイマ連動の切り替え機構(図外)により行う。
【0018】
上記の構成を採用することにより、流入口Iから流入した原水は、夾雑物除去槽Nで固液分離されつつ、流量調整槽B1を介して定量的に膜分離槽Eに移送され、膜分離槽Eで高度に浄水された後、消毒槽Qを介して浄化槽外へ定量排出される。
【0019】
さて、前述の吸引ポンプ9の下流側には、揚水配管101を介して給水部102としての屋根散水設備が接続されている。そして、冬には屋根上の雪の融雪に、夏には屋根の冷却の用に供される。
【0020】
〔別実施例〕
上記の実施例においては、前記給水部102が屋根に備えられる散水部である例を示したが、膜分離による被処理水は浄化度が高いため、空調用冷却水用もしくは手洗い用(例えば、トイレ用貯水タンクに給水)にも使用することができる。
また、第一、第二案内路G1,G2の切り替えは手動により各流路を開口、封止切り替えすることによって行っても良い。
【図面の簡単な説明】
【図1】 本発明の実施例における浄化槽の縦断側面図
【図2】 本発明の実施例における浄化槽の平膜支持構造の平面図
【符号の説明】
9 吸引ポンプ
E 膜分離槽
N 上流側槽に該当する夾雑物除去槽
B1 上流側槽に該当する流量調整槽
B2 上流側槽に該当する沈殿汚泥貯留槽
102 給水部
Q 消毒機構
G1 越流機構
G2,T 貯留機構
[0001]
BACKGROUND OF THE INVENTION
The present invention includes a membrane separation tank that sucks water to be treated and permeates the filtration membrane, and has an upstream tank that biologically treats the water to be treated supplied to the membrane separation tank in advance, and the membrane that has passed through the filtration membrane The present invention relates to a septic tank that includes a water supply mechanism that enables supply of permeated treated water to a water supply unit, and is provided with a disinfection mechanism that disinfects the membrane permeated treated water supplied to the water supply unit.
[0002]
[Prior art]
Conventionally, as this type of septic tank, the water to be treated that has flowed into the septic tank is received as it is in the upstream tank, and the entire amount passes through the filtration membrane and can be supplied to the water supply unit. What has been proposed.
[0003]
[Problems to be solved by the invention]
However, the water to be treated that flows into the septic tank is not necessarily biologically treated in advance in the upstream tank, and low-load treated water such as bath drainage (hereinafter referred to as low-load treated water). In some cases, it merely compresses the volume in the septic tank and delays the treatment of the water to be treated in the water purification facility. Here, in the case where the inflow of the water to be treated is continuous, the water level in the tank may rise too much and exceed the membrane filtration treatment capacity. In addition, when such a large amount of water to be treated is received, the water to be treated in the upstream side tank is in an oxygen-enriched state, which is liable to adversely affect the preliminary biological treatment. The treated water that has flowed in causes the sedimentation sludge and the like in the upstream tank to flow away and flow into the membrane separation tank, which may adversely affect the membrane separation tank.
[0004]
In addition, there are many cases in which the time for demand for membrane filtration treated water is limited to a part of the time of the day. In some cases, it could not be used effectively because it had to be released.
[0005]
Accordingly, an object of the present invention is to provide a septic tank that does not adversely affect the water treatment environment even when receiving a large inflow of water to be treated, and that can effectively use membrane permeation treated water. .
[0006]
[Means for Solving the Problems]
To achieve this object, the first characteristic configuration of the septic tank of the present invention includes an upstream tank for biologically treating the water to be treated in advance, and a membrane separation for sucking the biologically treated water to be permeated through the filtration membrane. A sterilization tank provided with a tank, a disinfection tank that disinfects the membrane permeation treated water that has passed through the filtration membrane, and a water supply mechanism that enables supply of the disinfected membrane permeation treated water to a water supply unit, A tank is provided in a tank separate from the upstream tank and the membrane separation tank, a flow medium is provided on the raw water inflow side of the upstream tank, and a convection pipe having an opening at the lower end is provided. An overflow mechanism for connecting the water to be treated, which sets the upstream tank to a predetermined water level or higher, to the disinfecting tank without passing through the membrane separation tank is connected to the upper end of the tank.
The second characteristic configuration of the purification tank of the present invention includes a membrane separation tank that sucks water to be treated and permeates the filtration membrane, and includes an upstream tank that biologically treats the water to be treated supplied to the membrane separation tank in advance. A septic tank provided with a water supply mechanism capable of supplying the membrane permeate treated water that has passed through the filtration membrane to the water supply unit, and provided with a disinfection mechanism for disinfecting the membrane permeate treated water supplied to the water supply unit, A storage mechanism that allows temporary storage of treated water that makes a side tank above a predetermined water level, and water that makes the upstream tank above a predetermined water level can be supplied to the disinfection mechanism without going through the membrane separation tank An overflow mechanism is provided, and a switching mechanism is provided to selectively supply the treated water to the storage mechanism or the overflow mechanism.
[0007]
[Function and effect]
In other words, the septic tank equipped with a membrane separation tank that sucks the water to be treated and permeates the filtration membrane, because the membrane permeation treated water that has passed through the filtration membrane is substantially free of particulate components, The membrane permeation treated water can be reused. Here, the septic tank usually includes an upstream tank that biologically treats the water to be treated supplied to the membrane separation tank in advance, so that the load of the membrane separation tank is stabilized and the components of the water to be treated are long-term. Enables stable membrane separation treatment. Therefore, if a water supply mechanism that enables supply of the membrane permeated treated water that has passed through the filtration membrane to the water supply unit is provided, the purified membrane permeated treated water can be reused. At this time, if a disinfection mechanism for disinfecting the membrane permeation treatment water supplied to the water supply unit is provided, the reused membrane permeation treatment water can be prevented from adversely affecting the surrounding environment.
[0008]
Here, in order to stably supply the membrane permeation treated water , it is necessary that the water treatment in the tank and the treated water supply be stable. Therefore, the treated water that has flowed in a large amount is supplied by the overflow mechanism to the disinfection mechanism without passing through the membrane separation tank, so that the treated water that brings the upstream tank to a predetermined water level or higher is supplied, for example, Low-load treated water that can be reused only by disinfection can be supplied to the water supply unit. As a result, the upstream tank does not exceed the predetermined water level, and can maintain a stable water treatment capacity as the entire septic tank, and easily obtain membrane-permeated treated water supplied to a high level on the ground.
[0010]
Furthermore, a storage mechanism that allows temporary storage of treated water that makes the upstream tank above a predetermined water level, and the disinfection of the treated water that makes the upstream tank above a predetermined water level without going through the membrane separation tank If there is provided an overflow mechanism that enables supply to the mechanism and a switching mechanism that selectively supplies the treated water to the storage mechanism or the overflow mechanism, for example, the membrane filtered treated water In the case where there is a risk of receiving an inflow of low-load treated water when supplying water to the water supply unit, the supply destination of the low-load treated water is the storage mechanism, otherwise, or When the storage mechanism reaches the capacity limit, the supply destination of the low-load treated water is the overflow mechanism, so that the reclaimed water can be reliably supplied to the water supply unit, and stable water treatment can be realized.
[0011]
DETAILED DESCRIPTION OF THE INVENTION
Embodiments of the present invention will be described below with reference to the drawings.
The purification equipment shown in FIG. 1 includes a purification tank 100 having a configuration unique to the present application, a pumping pipe 101 and a water supply unit 102 connected to the purification tank 100. Here, in FIG. 1, the example in which the water supply part 102 is comprised as a watering part (watering equipment) to a roof is shown.
Now, the septic tank 100 will be described. This is such that the water to be treated is transferred from the upstream side to the contaminant removal tank N, the flow rate adjustment tank B1, the sedimentation sludge storage tank B2, and the membrane separation tank E in the order of description. Each tank is partitioned by a partition wall W. Here, the contaminant removal tank N, the flow rate adjustment tank B1, and the sedimented sludge storage tank B2 correspond to the upstream tank with respect to the membrane separation tank E.
[0012]
The contaminant removal tank N receives the raw water flowing in from the inlet I as treated water and separates solid components such as scum generated on the liquid surface and solid matter precipitated from the treated water, An anaerobic bacterium that anaerobically decomposes the water to be treated is cultivated inside the liquid component of the raw water so that it can be naturally transferred to the flow rate adjusting tank B1 .
In the figure, F is an advection pipe provided with an opening F1 at the center in the width direction of the contaminant removal tank N, and the water to be treated that has become above the reference water level of the contaminant removal tank N is filtered by the filter medium F2. And is configured to flow into the flow rate adjusting tank B1 from the opening. Further, the upper part of the advection pipe F is provided with first and second guide paths G1 and G2 for guiding the water to be treated that has reached a predetermined water level slightly above the reference water level to other than the flow rate adjusting tank B1. .
[0013]
The flow rate adjustment tank B1 includes a measuring device 1a and a transfer air lift pump 1b, temporarily stores the liquid component of the water to be treated that has naturally transferred from the contaminant removal tank N, and the membrane separation tank E It is formed so that it can be transferred almost quantitatively through the transfer pipe 1c.
[0014]
The membrane separation tank E purifies the treated water by filtering it with a flat membrane M as a plurality of filtration membranes, and aerobic decomposes the organic components of the treated water in the membrane separation tank E. Bacteria are grown. Furthermore, with the flat membrane M attached in the tank, an air diffuser D is provided below the flat membrane M to supply bubbles and prevent sludge and the like from adhering to the surface of the flat membrane M. Therefore, by performing aeration operation from the aeration tube D, oxygen can be supplied to the aerobic bacteria, and the surface of the flat membrane can be washed, so that the membrane separation performance of the flat membrane M can be maintained high.
[0015]
The flat membrane M as a filtration membrane is formed by adhering and forming a polyethylene filtration membrane member on both surfaces of an ABS resin support plate having a treated water conducting portion on the inside, and communicating with the treated water conducting portion. When the suction operation is performed from the nozzle 4 in a state where the flat membrane M is immersed in the water to be treated, the water to be treated passes through the filtration membrane member, and the filtration membrane member Sludge and the like in the treated water are removed, and the treated water that has been highly purified can be taken out. Here, the filtration membrane member 6 is a microfiltration membrane having a pore diameter of 0.4 μm or less, and by selecting a membrane having such a pore diameter, contamination within the membrane can be prevented for a long period of use, and long-term Maintenance-free operation is possible.
[0016]
The nozzle 4 is connected in communication with a suction pump 9, and water to be treated (hereinafter referred to as membrane permeation treated water ) subjected to membrane separation treatment by the flat membrane M by operating the suction pump 9 is provided outside the septic tank. It works as a water supply mechanism that feeds water to the water supply section while feeding to the disinfection tank Q as a disinfected mechanism. Here, as shown in the figure, the suction pump 9 is provided outside the septic tank side wall 103 to ensure the ease of maintenance, and the suction pump 9 is disposed at a position lower than the lowest water level of the membrane separation tank E. Has been. Therefore, even when the suction pump 9 is stopped, the water to be treated remains in the suction pump 9 and serves as priming water at the time of restart.
[0017]
The first guide path G1 provided in the advection tube F top is communicatively connected to the disinfecting chamber Q, to supply available-the disinfecting chamber Q without passing through the membrane separation tank E water to be treated It constitutes the overflow mechanism. When the water levels of the contaminant removal tank N and the flow rate adjustment tank B1 are high, the low-load treated water that has flowed in large quantities into the tank can be transferred to the disinfection tank Q as it is and used as reclaimed water. . Further, the second guide path G2, and the body of the septic tank 100 Yes and communicatively connected to the temporary reservoir T provided separately, even if as in the previous, wherein said low-load processing water in the daytime mass When there is a possibility that the water will flow in and merge with the water supply from the water pipe, the first guide path G1 is closed and the low-load treated water is stored in the temporary storage tank T. It is configured to be able to. The first and second guide paths G1 and G2 are switched by a timer-linked switching mechanism (not shown).
[0018]
By adopting the above-described configuration, the raw water flowing in from the inlet I is quantitatively transferred to the membrane separation tank E via the flow rate adjustment tank B1 while being solid-liquid separated in the contaminant removal tank N, and membrane separation is performed. After being highly purified in the tank E, it is discharged quantitatively outside the septic tank via the disinfection tank Q.
[0019]
Now, on the downstream side of the above-described suction pump 9, a roof watering facility as a water supply unit 102 is connected via a pumping pipe 101. It is used for melting snow on the roof in winter and for cooling the roof in summer.
[0020]
[Another Example]
In the above embodiment, the water supply unit 102 is an example of a water spray unit provided on the roof. However, since the water to be treated by membrane separation has a high degree of purification, it is used for cooling water for air conditioning or for hand washing (for example, It can also be used for water supply to toilet water storage tanks.
Further, the switching between the first and second guide paths G1, G2 may be performed by manually switching each channel to open and seal.
[Brief description of the drawings]
FIG. 1 is a longitudinal side view of a septic tank in an embodiment of the present invention. FIG. 2 is a plan view of a flat membrane support structure of a septic tank in an embodiment of the present invention.
9 Suction pump E Membrane separation tank N Contaminant removal tank corresponding to upstream tank
Flow adjustment tank corresponding to B1 upstream tank
Precipitation sludge storage tank 102 corresponding to B2 upstream tank Water supply part Q Disinfection mechanism G1 Overflow mechanism G2, T Storage mechanism

Claims (2)

被処理水をあらかじめ生物処理する上流側槽と、生物処理された前記被処理水を吸引して濾過膜を透過させる膜分離槽と、前記濾過膜を透過した膜透過処理水を消毒する消毒槽と、消毒された前記膜透過処理水を給水部に供給可能にする給水機構とを設けてある浄化槽であって、
前記消毒槽を前記上流側槽及び前記膜分離槽とは別槽に設け、
前記上流側槽における原水流入側に、内部に濾材を配して下端部に開口部のある移流管を設け、前記移流管の上端部に、前記上流側槽を所定水位以上にする前記被処理水を前記膜分離槽を介さずに前記消毒槽に供給する越流機構を連通接続してある浄化槽。
An upstream tank for biologically treating the water to be treated in advance, a membrane separation tank for sucking the biologically treated water to be permeated through the filtration membrane, and a disinfection tank for disinfecting the membrane-permeated treated water that has passed through the filtration membrane And a septic tank provided with a water supply mechanism capable of supplying the sterilized membrane permeation treated water to a water supply unit,
The disinfection tank is provided in a separate tank from the upstream tank and the membrane separation tank,
The upstream side tank is provided with an advection pipe with a filter medium disposed at the lower end portion thereof on the raw water inflow side, and the upper end portion of the advection pipe is configured to have the upstream side tank at a predetermined water level or higher. A septic tank in which an overflow mechanism for supplying water to the disinfection tank without passing through the membrane separation tank is connected in communication.
被処理水を吸引して濾過膜を透過させる膜分離槽を備え、前記膜分離槽に供給される被処理水をあらかじめ生物処理する上流側槽を備え、濾過膜を透過した膜透過処理水を給水部に供給可能にする給水機構を備え、前記給水部に供給する前記膜透過処理水を消毒する消毒機構を設けてある浄化槽であって、
前記上流側槽を所定水位以上にする被処理水を一時貯留可能にする貯留機構、及び、前記上流側槽を所定水位以上にする被処理水を前記膜分離槽を介さずに前記消毒機構に供給可能にする越流機構を設け、前記被処理水を前記貯留機構もしくは前記越流機構に択一的に供給切り替えする切り替え機構を設けてある浄化槽。
A membrane separation tank that sucks water to be treated and permeates the filtration membrane, an upstream tank that biologically treats the water to be treated that is supplied to the membrane separation tank, and has membrane permeation treated water that has passed through the filtration membrane. A septic tank provided with a water supply mechanism that enables supply to a water supply unit, and provided with a disinfection mechanism for disinfecting the membrane permeation treated water supplied to the water supply unit,
A storage mechanism that makes it possible to temporarily store water to be treated that makes the upstream tank above a predetermined water level, and a water treatment mechanism that makes the upstream tank above a predetermined water level to the disinfection mechanism without going through the membrane separation tank A septic tank provided with an overflow mechanism that enables supply, and a switching mechanism that selectively switches the supply of the treated water to the storage mechanism or the overflow mechanism.
JP09878399A 1999-04-06 1999-04-06 Septic tank Expired - Fee Related JP3688146B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11247924B2 (en) * 2016-05-16 2022-02-15 Dan Van Truong Apparatus for treating wastewater and a system for collecting and treating wastewater combining rainwater drainage

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US6863817B2 (en) 2002-12-05 2005-03-08 Zenon Environmental Inc. Membrane bioreactor, process and aerator
JP2005211747A (en) * 2004-01-28 2005-08-11 Hitachi Housetec Co Ltd Phosphorus removing apparatus-housed vessel and small-scaled sewage cleaning tank provided with the same
JP2008302279A (en) * 2007-06-06 2008-12-18 Fuji Clean Kogyo Kk Water treatment apparatus

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11247924B2 (en) * 2016-05-16 2022-02-15 Dan Van Truong Apparatus for treating wastewater and a system for collecting and treating wastewater combining rainwater drainage

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