JP3271882B2 - Septic tank - Google Patents
Septic tankInfo
- Publication number
- JP3271882B2 JP3271882B2 JP29505795A JP29505795A JP3271882B2 JP 3271882 B2 JP3271882 B2 JP 3271882B2 JP 29505795 A JP29505795 A JP 29505795A JP 29505795 A JP29505795 A JP 29505795A JP 3271882 B2 JP3271882 B2 JP 3271882B2
- Authority
- JP
- Japan
- Prior art keywords
- tank
- storage tank
- water
- sludge
- sludge storage
- 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.)
- Expired - Lifetime
Links
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
- Treatment Of Biological Wastes In General (AREA)
Description
【0001】[0001]
【発明の属する技術分野】本発明は、槽内に発生する汚
泥を貯留する汚泥貯留槽を設けた浄化槽に関する。[0001] The present invention relates to a purification tank provided with a sludge storage tank for storing sludge generated in the tank.
【0002】[0002]
【従来の技術】従来、この種の浄化槽においては、汚泥
貯留槽は単に汚泥貯留用の空間を設けてあるだけであっ
た。2. Description of the Related Art Conventionally, in this type of septic tank, the sludge storage tank is simply provided with a space for storing sludge.
【0003】[0003]
【発明が解決しようとする課題】通常、汚泥貯留槽に貯
留された汚泥は、定期的に槽外へ引き抜き操作すること
により、槽内の汚泥量の増加を抑制出来る構成にしてあ
るものの、上述した従来の汚泥貯留槽によれば、単に汚
泥を貯留するだけの構成となっているため、たとえ静置
して沈殿濃縮したとしても、汚泥を高濃度にする事は難
しく、低濃度で汚泥を引き抜くことになると、所定量の
固形成分を引き抜くにも大量の汚泥を引き抜かねばなら
ず、頻繁に汚泥引き抜きを行わねばならなくなるなど、
メンテナンスに多大な労力を費やさねばならないという
欠点があった。Usually, the sludge stored in the sludge storage tank is configured to be able to suppress an increase in the amount of sludge in the tank by periodically pulling the sludge out of the tank. According to the conventional sludge storage tank described above, since it is configured to simply store sludge, it is difficult to increase the concentration of sludge even if it is allowed to settle and sediment even if it is allowed to stand still. When it comes to withdrawing, a large amount of sludge must be extracted to extract a predetermined amount of solid components, and frequent sludge extraction must be performed.
The disadvantage is that a great deal of labor has to be spent on maintenance.
【0004】従って、本発明の目的は、上記欠点に鑑
み、汚泥を高濃度に濃縮したのち引き抜き操作すること
の出来る浄化槽を提供することにある。[0004] Accordingly, an object of the present invention is to provide a septic tank capable of performing a drawing operation after concentrating sludge at a high concentration in view of the above-mentioned drawbacks.
【0005】[0005]
【課題を解決するための手段】この目的を達成するため
の本発明の特徴構成は、前記汚泥貯留槽(N2)上部に
被処理水を濾過する濾過膜装置(C1)を内装するとと
もに、前記汚泥貯留槽(N2)から汚泥貯留槽(N2)
に隣接する他の槽に前記濾過膜装置(C1)で濾過済の
濾過水を移送する濾過水移送管(A6)を設けて、前記
濾過膜装置(C1)に連設し、前記汚泥貯留槽(N2)
の水位を、前記他の槽の水位よりも高く設定し、前記被
処理水移送管(A6)を、前記汚泥貯留槽(N2)の水
位以下に設けるとともに、前記濾過膜装置(C1)の下
方に散気管(D1)を設け、前記濾過膜装置(C1)の
下方に供給される被処理水を固液分離するスクリーン
(C3)を設け、前記スクリーン(C3)の下方には、
前記スクリーン(C3)に気泡を供給する散気装置(D
2)を設けてある点にある。また、汚泥貯留槽(N2)
および膜分離槽(E2)および汚泥貯留槽(N2)に隣
接する他の槽を設けた浄化槽であって、前記他の槽から
の被処理水を固液分離してえられた固形物を前記汚泥貯
留槽 (N2)に移送するスクリーン濾過装置(S)を設
け、前記膜分離槽(E2)底部に沈殿する沈殿汚泥を前
記汚泥貯留槽(N2)に返送する沈殿汚泥移送管(A
4)を設け、前記汚泥貯留槽(N2)上部に被処理水を
濾過する濾過膜装置(C1)を内装するとともに、前記
汚泥貯留槽(N2)から汚泥貯留槽(N2)に隣接する
他の槽に前記濾過膜装置(C1)で濾過済の濾過水を移
送する濾過水移送管(A6)を設けて、前記濾過膜装置
(C1)に連設してあってもよく、汚泥貯留槽(N2)
および膜分離槽(E2)および汚泥貯留槽(N2)に隣
接する他の槽を設けた浄化槽であって、前記他の槽から
の被処理水を固液分離してえられた固形物を前記汚泥貯
留槽 (N2)に移送するスクリーン濾過装置(S)を設
け、前記膜分離槽(E2)底部に沈殿する沈殿汚泥を前
記汚泥貯留槽(N2)に返 送する沈殿汚泥移送管(A
4)を設け、前記汚泥貯留槽(N2)上部に被処理水を
濾過する濾過膜装置(C1)を内装するとともに、前記
汚泥貯留槽(N2)から汚泥貯留槽(N2)に隣接する
他の槽に前記濾過膜装置(C1)で濾過済の濾過水を移
送する濾過水移送管(A6)を設けて、前記濾過膜装置
(C1)に連設し、前記汚泥貯留槽(N2)の水位を、
前記他の槽の水位よりも高く設定し、前記被処理水移送
管(A6)を、前記汚泥貯留槽(N2)の水位以下に設
けるとともに、前記濾過膜装置(C1)の下方に散気管
(D1)を設け、前記濾過膜装置(C1)の下方に供給
される被処理水を固液分離するスクリーン(C3)を設
け、前記スクリーン(C3)の下方には、前記スクリー
ン(C3)に気泡を供給する散気装置(D2)を設けて
あってもよい。その作用・効果は以下の通りである。To achieve the above object, the present invention is characterized in that a filtration membrane device (C1) for filtering water to be treated is provided above the sludge storage tank (N2), Sludge storage tank (N2) to sludge storage tank (N2)
A filtration water transfer pipe (A6) for transferring filtered water filtered by the filtration membrane device (C1) to another tank adjacent to the filtration membrane device (C1), and connected to the filtration membrane device (C1); (N2)
Water level of the other tank is set higher than the water level of the other tank.
Transfer the treated water transfer pipe (A6) to the water in the sludge storage tank (N2).
And below the filtration membrane device (C1).
A diffuser tube (D1) is provided on the side of the filter membrane device (C1).
Screen for solid-liquid separation of water to be treated supplied below
(C3), and below the screen (C3),
A diffuser (D) for supplying air bubbles to the screen (C3)
2) . In addition, sludge storage tank (N2)
And next to membrane separation tank (E2) and sludge storage tank (N2)
A septic tank provided with another tank in contact with the tank,
The solids obtained by solid-liquid separation of the water to be treated
A screen filtration device (S) for transferring to the detention tank (N2) is installed.
And a settling sludge transfer pipe (A) for returning the settled sludge settled at the bottom of the membrane separation tank (E2) to the sludge storage tank (N2).
4), a filtration membrane device (C1) for filtering the water to be treated is installed above the sludge storage tank (N2), and another from the sludge storage tank (N2) adjacent to the sludge storage tank (N2). The tank may be provided with a filtered water transfer pipe (A6) for transferring filtered water filtered by the filtration membrane device (C1), and may be connected to the filtration membrane device (C1). N2)
And next to membrane separation tank (E2) and sludge storage tank (N2)
A septic tank provided with another tank in contact with the tank,
The solids obtained by solid-liquid separation of the water to be treated
A screen filtration device (S) for transferring to the detention tank (N2) is installed.
The sludge settling at the bottom of the membrane separation tank (E2).
Serial sludge storage tank (N2) Return sent to precipitate the sludge transfer pipe (A
4), a filtration membrane device (C1) for filtering the water to be treated is installed above the sludge storage tank (N2), and another from the sludge storage tank (N2) adjacent to the sludge storage tank (N2). The tank is provided with a filtered water transfer pipe (A6) for transferring filtered water filtered by the filtration membrane device (C1), and is connected to the filtration membrane device (C1), and a water level of the sludge storage tank (N2) is provided. To
Set the water level higher than the other tank, and transfer the water to be treated.
Install the pipe (A6) below the water level of the sludge storage tank (N2).
And a diffuser below the filtration membrane device (C1).
(D1) provided and supplied below the filtration membrane device (C1)
Screen (C3) for solid-liquid separation of treated water
Below the screen (C3).
A diffuser (D2) for supplying air bubbles to the housing (C3) may be provided . The operation and effect are as follows.
【0006】〔作用効果〕つまり、上述の構成により、
前記濾過膜装置で汚泥貯留槽内の汚泥を固液分離するか
ら、汚泥貯留槽内から水分を他の水処理槽へ引き抜き、
水処理に供することが出来、また、固液分離された固形
成分は、前記汚泥貯留槽内に残留するので、前記汚泥貯
留槽内の汚泥を高濃度に濃縮することが出来る。従っ
て、浄化槽をメンテナンスするときには前記汚泥貯留槽
内のの汚泥を引き抜くのに、高濃度の状態で引き抜きで
きて、少ない引き抜き量でも浄化槽内の汚泥を十分除去
できる。また、汚泥を高濃度な状態で蓄積するものであ
るから小さな汚泥貯留槽であっても、長期にわたって汚
泥の蓄積を許容できるから、メンテナンスをあまり行わ
ずとも浄化槽を安定運転する事が出来るようになって、
メンテナンスに要する労力を軽減出来るとともに、浄化
槽を全体として小さなものとでき、浄化槽の施工等を容
易に出来る。[Effects] That is, according to the above-described structure,
Since the sludge in the sludge storage tank is solid-liquid separated by the filtration membrane device, water is extracted from the sludge storage tank to another water treatment tank,
Since the solid component that can be subjected to water treatment and solid-liquid separated remains in the sludge storage tank, the sludge in the sludge storage tank can be concentrated to a high concentration. Therefore, when the septic tank is maintained, the sludge in the sludge storage tank can be extracted in a high-concentration state, and the sludge in the septic tank can be sufficiently removed with a small amount of extraction. In addition, since sludge is accumulated in a high concentration state, even a small sludge storage tank can accumulate sludge for a long time, so that the septic tank can be operated stably without much maintenance. Become,
The labor required for maintenance can be reduced, and the septic tank can be made small as a whole, so that the construction of the septic tank can be facilitated.
【0007】また、前記濾過膜装置は、前記汚泥貯留槽
上方に配置してあれば、前記汚泥貯留槽で沈殿濃縮され
た汚泥の上澄液を固液分離することが出来、効率よく汚
泥濃縮を行うことが出来る。また、前記汚泥貯留槽の水
位を、前記他の槽の水位よりも高く設定し、前記被処理
水移送管を、前記汚泥貯留槽の水位以下に設けてあれ
ば、特に前記濾過膜装置に吸引濾過膜装置を設けること
無く、前記汚泥貯留槽の汚泥を常時濃縮運転することが
出来る。この構成において、前記濾過膜装置の下方に散
気管を設けてあれば、前記濾過膜装置に汚れが付着して
も、前記散気装置による気泡が前記濾過膜装置に衝突す
るから、前記気泡が前記濾過膜装置から汚れを剥離させ
つつ、前記濾過膜装置に汚れが定着するのを防止するの
で、被処理水を濃縮する機能を長期にわたって維持する
ことが出来る。尚、前記汚泥貯留槽においては、臭気が
発生しやすいが、散気による前記気泡は、臭気の除去に
も役立つ。また濾過膜装置の下方に固液分離用のスクリ
ーンを設けてあれば、比較的大きな固形成分が前記濾過
膜装置に付着するのを防止でき、前記濾過膜装置が目詰
まりする等の不都合を防止しやすい。また、前記スクリ
ーンの下方に前記スクリーンに気泡を供給する散気装置
を設けてあれば、前記汚泥貯留槽の汚泥上澄に上昇流を
形成させ、前記濾過装置や前記スクリーンに付着した汚
れを剥離させるとともに、前記汚泥貯留槽内の臭気成分
を酸化除去して緩和させられる。なお、汚泥貯留槽およ
び膜分離槽および汚泥貯留槽に隣接する他の槽を設けて
ある浄化槽にあっては、前記他の槽からの被処理水を固
液分離してえられた固形物を前記汚泥貯留槽に移送する
スクリーン濾過装置を設けることによって、前記他の槽
からは固形物を優先的に汚泥貯留槽に移送、貯留させ、
固形成分をより高濃度に貯留できるようになる。 前記膜
分離槽底部に沈殿する沈殿汚泥を前記汚泥貯留槽に返送
する沈殿汚泥移送管を設けてあれば、固形物を主成分と
する沈殿汚泥を前記汚泥貯留槽に沈殿濃縮できて、前記
膜分離槽における水処理に悪影響を及ぼす虞のある成分
を貯留し 、沈殿濃縮することができる。 Further, if the filtration membrane device is disposed above the sludge storage tank, the supernatant of the sludge precipitated and concentrated in the sludge storage tank can be separated into solid and liquid, and the sludge concentration can be efficiently performed. Can be performed. Further, if the water level of the sludge storage tank is set higher than the water level of the other tank, and the treated water transfer pipe is provided at a level lower than the water level of the sludge storage tank, suction is particularly performed to the filtration membrane device. Without providing a filtration membrane device, the sludge in the sludge storage tank can be constantly concentrated. In this configuration, if an air diffuser is provided below the filtration membrane device, even if dirt adheres to the filtration membrane device, the bubbles generated by the air diffusion device collide with the filtration membrane device. Since the dirt is prevented from being fixed to the filtration membrane device while the dirt is being stripped from the filtration membrane device, the function of concentrating the water to be treated can be maintained for a long time. In the sludge storage tank, odor is likely to be generated, but the air bubbles due to diffused air also help to remove odor. In addition, if a screen for solid-liquid separation is provided below the filtration membrane device, it is possible to prevent relatively large solid components from adhering to the filtration membrane device and to prevent inconvenience such as clogging of the filtration membrane device. It's easy to do. In addition, the script
Diffuser for supplying air bubbles to the screen below the screen
If an upflow is established in the sludge supernatant in the sludge storage tank,
Formed on the filter and the screen.
Odor components in the sludge storage tank
Can be relaxed by oxidative removal. The sludge storage tank and
And other tanks adjacent to the membrane separation tank and sludge storage tank
In a certain septic tank, the water to be treated from the other tank is fixed.
Transfer the solid obtained by liquid separation to the sludge storage tank
By providing a screen filtration device, the other tank
From which the solid matter is preferentially transferred to the sludge storage tank and stored,
The solid component can be stored at a higher concentration. The membrane
Settled sludge settling at the bottom of the separation tank is returned to the sludge storage tank
Solids as the main component
The sedimentation sludge to be deposited and concentrated in the sludge storage tank,
Components that may adversely affect water treatment in the membrane separation tank
Can be stored and concentrated by precipitation.
【0008】[0008]
【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に示すように、本発明の浄化
槽は、円筒状の浄化槽本体Xの両端を鏡部X1,X2を
設けて内部に密閉空間を形成するとともに、内部の密閉
空間に仕切り壁を設けて区分けして、上流側から、流量
調整槽N1、脱窒素槽E1、汚泥貯留槽N2、膜分離槽
E2、放流ポンプ槽Tを形成してあり、前記各槽の上部
には、メンテナンス等に用いるマンホールHを設けてあ
る。Embodiments of the present invention will be described below with reference to the drawings. As shown in FIG. 1, the septic tank of the present invention is provided with mirror sections X1 and X2 at both ends of a cylindrical septic tank main body X to form an enclosed space inside, and is provided with a partition wall in the enclosed space. Then, from the upstream side, a flow control tank N1, a denitrification tank E1, a sludge storage tank N2, a membrane separation tank E2, and a discharge pump tank T are formed, and a manhole used for maintenance and the like is provided above each of the tanks. H is provided.
【0009】前記流量調整槽N1は、前記浄化槽本体X
の一方の鏡部X1に設けてなる流入口Iから浄化槽内に
流入した被処理水の原水を受けて、その被処理水中の夾
雑物を沈殿除去しつつ、内部に生育する嫌気性菌によ
り、被処理水を嫌気処理しつつ、被処理水を一時貯留す
る水処理室内に、被処理水を脱窒素槽E1に移送する第
一ポンプP1を設け、被処理水が大量に流入した場合
や、長期にわたって被処理水の流入が無い場合にも、被
処理水を定常的に脱窒素槽E1に移送して、後続の各水
処理室での水処理に支障をきたさないようにしてある。The flow control tank N1 is provided with the purifying tank main body X.
An anaerobic bacterium that grows inside receives the raw water to be treated that has flowed into the septic tank from the inflow port I provided in one of the mirror parts X1 and precipitates and removes impurities in the treated water. A first pump P1 for transferring the water to be treated to the denitrification tank E1 is provided in the water treatment chamber for temporarily storing the water to be treated while performing the anaerobic treatment of the water to be treated, Even when there is no inflow of the water to be treated for a long period of time, the water to be treated is constantly transferred to the denitrification tank E1 so as not to hinder the water treatment in each of the subsequent water treatment chambers.
【0010】前記脱窒素槽E1は、前記流量調整槽N1
に隣接する水処理室に、前記流量調整槽N1からの被処
理水を流入させる流入管A1を、前記第一ポンプP1に
接続して設け、被処理水の流入路を構成してある。ま
た、第二ポンプP2を内装し、その第二ポンプP2に移
送管A2を設け、被処理水を前記膜分離槽E2へ移送す
る構成にしてある。また、槽内の被処理水を攪拌循環さ
せる攪拌ポンプP3を内装してあり、槽内の被処理水の
混合を図り、BOD負荷の高い被処理水と、硝化済の被
処理水とを混合し、高度な脱窒処理を行える構成にして
ある。The denitrification tank E1 is provided with the flow control tank N1.
An inflow pipe A1 for inflowing the water to be treated from the flow rate adjusting tank N1 into the water treatment chamber adjacent to the first pump P1 is provided to form an inflow passage of the water to be treated. Further, a second pump P2 is provided inside, and a transfer pipe A2 is provided in the second pump P2 to transfer the water to be treated to the membrane separation tank E2. In addition, a stirring pump P3 for stirring and circulating the water to be treated in the tank is provided to mix the water to be treated in the tank and mix the water to be treated with a high BOD load with the nitrified water to be treated. In addition, it is configured to perform advanced denitrification processing.
【0011】前記膜分離槽E2は、前記脱窒素槽E1と
の間を仕切る隔壁に、前記流入路を設けるとともに、前
記脱窒素槽E1から過剰に流入した被処理水を前記脱窒
素槽E1に返送する返送管A3を設けて、被処理水の返
送路を構成してある。また、多数の平板状の濾過膜板を
直立状態で平行に並設してなる膜分離装置Mを内装して
なり、前記膜分離装置Mは、濾過膜板の多数を整列して
保持する濾過膜板保持枠を設け、下部に前記濾過膜板保
持枠を支持する脚部を設け、前記脚部間にその濾過膜板
に気泡を供給して、その膜面に汚泥等の付着しすぎるの
を防止し、かつ、前記膜分離槽E2内に循環流を形成し
ながら被処理水に酸素を供給する散気装置Dを内装して
構成してある。また、前記膜分離装置Mのそれぞれの濾
過膜板には取水管M1を連設するとともに、前記取水管
M1からの濾過水を合流させて膜分離槽E2外へ導く集
水管M2を接続してあり、前記膜分離槽E2の水面より
も下方で前記膜分離槽E2に隣接する放流ポンプ槽Tに
連通接続してある。また、前記膜分離槽E2には、沈殿
汚泥をエアリフト作用によって前記汚泥貯留槽N2に移
送する沈殿汚泥移送管A4を内装してある。In the membrane separation tank E2, the inflow path is provided in a partition separating the denitrification tank E1, and the water to be treated excessively flowing from the denitrification tank E1 is supplied to the denitrification tank E1. A return pipe A3 for returning is provided to constitute a return path of the water to be treated. Further, a membrane separation device M in which a large number of flat filtration membrane plates are arranged in parallel in an upright state is installed, and the membrane separation device M is a filtration device that aligns and holds a large number of filtration membrane plates. A membrane plate holding frame is provided, and a leg for supporting the filtration membrane plate holding frame is provided at a lower portion, and air bubbles are supplied to the filtration membrane plate between the legs, so that sludge or the like adheres excessively to the membrane surface. And a diffuser D for supplying oxygen to the water to be treated while forming a circulating flow in the membrane separation tank E2. In addition, an intake pipe M1 is connected to each filtration membrane plate of the membrane separation device M, and a water collection pipe M2 that joins filtered water from the intake pipe M1 and guides the filtered water to the outside of the membrane separation tank E2 is connected. In addition, it is connected to a discharge pump tank T adjacent to the membrane separation tank E2 below the water surface of the membrane separation tank E2. Further, the membrane separation tank E2 is provided with a settling sludge transfer pipe A4 for transferring the settled sludge to the sludge storage tank N2 by an air lift action.
【0012】前記汚泥貯留槽N2は、前記脱窒素槽E1
と、前記膜分離槽E2との間に水処理空間を区分けして
設けてある。前記汚泥貯留槽N2の上方には前記脱窒素
槽E1から、膜分離槽E2に被処理水を移送する移送管
A2を横架姿勢で配置してある。前記移送管A2の、前
記汚泥貯留槽N2上方部分には、固液分離用のスクリー
ン濾過装置Sを介装してある。前記スクリーン濾過装置
Sは、図2,3に示すように、固液分離用の多数の櫛歯
S1aを備えてなる櫛型スクリーンS1と、前記櫛歯S
1a間に多数の突起S2aを挿通させて前記櫛型スクリ
ーンS1に引っ掛かった固形物をかきとるローラーS2
とを備えてなり、前記移送管A2を介して移送される被
処理水のうち、比較的大きな固形成分を前記櫛型スクリ
ーンS1で濾過するとともに、前記櫛歯S1aを通過し
た被処理水を前記膜分離槽E2に移送させ、かつ、前記
櫛歯S1aに引っ掛かった固形物は、前記ローラーS2
によって上方にかきあげられ、最終的に前記汚泥貯留槽
N2に落下させられる構成にしてあり、前記固形物は前
記汚泥貯留槽内に蓄積される。また、前記沈殿汚泥移送
管A4は、前記膜分離槽E2と前記汚泥貯留槽N2の間
にわたって設けてあり、前記膜分離槽E2底部に沈殿す
る比較的高濃度の沈殿汚泥は、前記沈殿汚泥移送管A4
によって、前記汚泥貯留槽N2に返送され貯留される構
成にしてある。さらに、図1に示すように、前記汚泥貯
留槽N2の上部には、被処理水を濾過する濾過膜装置C
1を内装するとともに、前記汚泥貯留槽N2から脱窒素
槽E1に前記濾過膜装置C1で濾過済の濾過水を移送す
る濾過水移送管A6を設けて、前記濾過膜装置C1に連
設してある。また、前記濾過膜装置C1は、上下両端を
開放状態にしてあるケーシングC2で覆うとともに、そ
のケーシングC2の下部開口には、パンチングメタルか
らなるスクリーンC3を設けて、粗大な固形成分が前記
濾過膜装置C1に付着するのを防止するように構成して
ある。前記ケーシングC2内で前記濾過膜装置C1の下
方には前記濾過膜装置C1に気泡を供給する散気装置D
1を設け、前記スクリーンC3の下方には、前記スクリ
ーンC3に気泡を供給する散気装置D2を設けて、汚泥
上澄に上昇流を形成させ、前記濾過膜装置C1や、前記
スクリーンC3に付着した汚れを剥離させるとともに、
前記汚泥貯留槽N2内の臭気成分を酸化除去して緩和可
能にする構成にしてある。尚、前記汚泥貯留槽N2の水
位は、通常脱窒素槽E1の水位よりも高くなるように設
定してあるとともに、濾過水移送管A6には逆止弁A7
を設けて脱窒素槽E1の被処理水が逆流するのを防止し
てある。The sludge storage tank N2 is provided with the denitrification tank E1.
And the membrane separation tank E2, a water treatment space is provided separately. Above the sludge storage tank N2, a transfer pipe A2 for transferring the water to be treated from the denitrification tank E1 to the membrane separation tank E2 is disposed in a horizontal posture. A screen filtration device S for solid-liquid separation is provided above the sludge storage tank N2 of the transfer pipe A2. As shown in FIGS. 2 and 3, the screen filtering device S includes a comb-shaped screen S1 including a plurality of comb teeth S1a for solid-liquid separation;
A roller S2 that scrapes solid matter caught on the comb-shaped screen S1 by inserting a large number of protrusions S2a between 1a.
Among the water to be treated transferred through the transfer pipe A2, a relatively large solid component is filtered by the comb screen S1, and the water to be treated that has passed through the comb teeth S1a is The solid matter transferred to the membrane separation tank E2 and caught on the comb teeth S1a is transferred to the roller S2.
, And finally dropped into the sludge storage tank N2, and the solid matter is accumulated in the sludge storage tank. Further, the settling sludge transfer pipe A4 is provided between the membrane separation tank E2 and the sludge storage tank N2, and the relatively high concentration of settled sludge settled at the bottom of the membrane separation tank E2 is transferred to the settling sludge. Tube A4
Thus, the sludge is returned to and stored in the sludge storage tank N2. Further, as shown in FIG. 1, a filtration membrane device C for filtering the water to be treated is provided above the sludge storage tank N2.
1 and a filtered water transfer pipe A6 for transferring filtered water filtered by the filtration membrane device C1 from the sludge storage tank N2 to the denitrification tank E1. The filtration water transfer tube A6 is connected to the filtration membrane device C1. is there. The filtration membrane device C1 is covered with a casing C2 whose upper and lower ends are open, and a screen C3 made of punched metal is provided at a lower opening of the casing C2 so that coarse solid components can be removed by the filtration membrane. The device is configured to prevent it from adhering to the device C1. An air diffuser D that supplies air bubbles to the filtration membrane device C1 below the filtration membrane device C1 in the casing C2.
1 is provided below the screen C3, and an air diffuser D2 for supplying air bubbles to the screen C3 is provided to form an upward flow in the sludge supernatant and adhere to the filtration membrane device C1 and the screen C3. While removing the dirt
The configuration is such that the odor components in the sludge storage tank N2 can be mitigated by oxidative removal. Incidentally, the water level of the sludge storage tank N2 is set to be higher than the water level of the normal denitrification tank E1, and a check valve A7 is connected to the filtrate water transfer pipe A6.
Is provided to prevent the water to be treated in the denitrification tank E1 from flowing backward.
【0013】この様な構成により、前記汚泥貯留槽N2
内には、前記スクリーン濾過装置Sからの固形成分や、
前記膜分離槽E2からの沈殿汚泥等(以下単に汚泥等と
略称する)、水処理上に悪影響を及ぼす虞のある成分を
貯留し、沈殿濃縮するとともに、前記濾過膜装置C1に
より、前記汚泥貯留槽N2と、脱窒素槽E1との水頭差
によって前記汚泥貯留槽N2の上澄から固液分離した濾
過水を前記脱窒素槽E2に返送することによって、さら
に濃縮可能な構成となり、固形成分を高濃度に貯留する
ことが出来るようになり、汚泥等の引き抜き操作を行う
時には、効率よく行えるようになった。With such a configuration, the sludge storage tank N2
Inside, the solid components from the screen filtration device S,
The sludge from the membrane separation tank E2 and the like (hereinafter simply referred to as sludge and the like) and components that may adversely affect water treatment are stored, sedimented and concentrated, and the sludge storage is performed by the filtration membrane device C1. By returning the filtered water solid-liquid separated from the supernatant of the sludge storage tank N2 to the denitrification tank E2 due to the head difference between the tank N2 and the denitrification tank E1, it becomes possible to further concentrate the solid component. It can be stored at a high concentration, and can be efficiently performed when pulling out sludge or the like.
【0014】前記放流ポンプ槽Tは、消毒槽Q1と、貯
留槽Q2とからなり、前記消毒槽Q1は、前記膜分離槽
E2と、前記放流ポンプ槽Tとを仕切る隔壁に処理水受
け容器を設け、その壁面に小孔を設けて構成してあり、
前記消毒槽Q1に流入した濾過水は、消毒されたのち貯
留槽Q2に流入する。前記貯留槽Q2は、第三ポンプP
4を内装してあり、前記処理水を貯留したのち、放流ポ
ンプP1で処理水を汲み上げ、排出管A5を介して放流
口Zから浄化槽外へ放流可能に構成してある。これによ
り、消毒済の処理水が前記貯留槽Tからほぼ定量的に浄
化槽外に放流される。The discharge pump tank T comprises a disinfecting tank Q1 and a storage tank Q2. The disinfecting tank Q1 has a treated water receiving container on a partition separating the membrane separation tank E2 and the discharge pump tank T. It is configured by providing a small hole in the wall surface,
The filtered water that has flowed into the disinfection tank Q1 flows into the storage tank Q2 after being disinfected. The storage tank Q2 is provided with a third pump P
After storing the treated water, the treated water is pumped up by the discharge pump P1 and discharged from the discharge port Z to the outside of the purification tank via the discharge pipe A5. Thereby, the disinfected treated water is almost quantitatively discharged from the storage tank T to the outside of the purification tank.
【0015】尚、特許請求の範囲の項に、図面との対照
を便利にするために符号を記すが、該記入により本発明
は添付図面の構成に限定されるものではない。In the claims, reference numerals are provided for convenience of comparison with the drawings, but the present invention is not limited to the configuration shown in the attached drawings.
【図1】浄化槽の縦断側面図FIG. 1 is a vertical side view of a septic tank.
【図2】スクリーン濾過装置の全体斜視図FIG. 2 is an overall perspective view of a screen filtration device.
【図3】スクリーン濾過装置の要部平面図FIG. 3 is a plan view of a main part of the screen filtration device.
A6 被処理水移送管 C1 濾過膜装置 C3 スクリーン D1 散気管 N2 汚泥貯留槽 A6 Treated water transfer pipe C1 Filtration membrane device C3 Screen D1 Aeration pipe N2 Sludge storage tank
───────────────────────────────────────────────────── フロントページの続き (72)発明者 本田 和之 滋賀県甲賀郡甲西町高松2番地の1 株 式会社クボタ 滋賀工場内 (72)発明者 浜田 勝己 滋賀県甲賀郡甲西町高松2番地の1 株 式会社クボタ 滋賀工場内 (72)発明者 古瀬 真一 滋賀県甲賀郡甲西町高松2番地の1 株 式会社クボタ 滋賀工場内 (56)参考文献 特開 平7−256294(JP,A) 特開 平6−179000(JP,A) 特開 平4−341394(JP,A) 特開 平3−114585(JP,A) 特開 平7−290075(JP,A) 実開 平4−57202(JP,U) (58)調査した分野(Int.Cl.7,DB名) C02F 3/00 ──────────────────────────────────────────────────続 き Continuing from the front page (72) Inventor Kazuyuki Honda 1 at 2, Takamatsu, Kosai-cho, Koga-gun, Koka-gun, Shiga Prefecture Inside the Kubota Shiga Plant (72) Katsumi Hamada 2, Takamatsu, Kosai-cho, Koga-gun, Shiga (1) Inside Kubota Shiga Plant, Ltd. (72) Inventor Shinichi Furuse Inside Kubota Shiga Plant, 2 at Takamatsu, Kosai-cho, Koga-gun, Shiga Prefecture (56) References JP-A-7-256294 (JP, A) JP-A-6-179000 (JP, A) JP-A-4-341394 (JP, A) JP-A-3-114585 (JP, A) JP-A-7-290075 (JP, A) JP-A-4-57202 ( JP, U) (58) Field surveyed (Int. Cl. 7 , DB name) C02F 3/00
Claims (3)
って、 前記汚泥貯留槽(N2)上部に被処理水を濾過する濾過
膜装置(C1)を内装するとともに、前記汚泥貯留槽
(N2)から汚泥貯留槽(N2)に隣接する他の槽に前
記濾過膜装置(C1)で濾過済の濾過水を移送する濾過
水移送管(A6)を設けて、前記濾過膜装置(C1)に
連設し、 前記汚泥貯留槽(N2)の水位を、前記他の槽の水位よ
りも高く設定し、 前記被処理水移送管(A6)を、前記汚泥貯留槽(N
2)の水位以下に設けるとともに、 前記濾過膜装置(C1)の下方に散気管(D1)を設
け、前記濾過膜装置(C1)の下方に供給される被処理
水を固液分離するスクリーン(C3)を設け、 前記スクリーン(C3)の下方には、前記スクリーン
(C3)に気泡を供給する散気装置(D2)を設け てあ
る浄化槽。1. A purification tank provided with a sludge storage tank (N2), wherein a filtration membrane device (C1) for filtering water to be treated is installed above the sludge storage tank (N2), and the sludge storage tank (N2) is provided. A filtration water transfer pipe (A6) for transferring filtered water filtered by the filtration membrane device (C1) is provided from N2) to another tank adjacent to the sludge storage tank (N2), and the filtration membrane device (C1) is provided. continuously provided in, the water level of the sludge storage tank (N2), the water level of the other tank
And the treated water transfer pipe (A6) is connected to the sludge storage tank (N
A water diffuser (D1) is installed below the filtration membrane device (C1) while being provided below the water level of 2).
The processing target supplied below the filtration membrane device (C1)
A screen (C3) for solid-liquid separation of water is provided, and the screen (C3) is provided below the screen (C3).
A septic tank provided with a diffuser (D2) for supplying air bubbles to (C3) .
2)および汚泥貯留槽(N2)に隣接する他の槽を設け
た浄化槽であって、 前記他の槽からの被処理水を固液分離してえられた固形
物を前記汚泥貯留槽 (N2)に移送するスクリーン濾過
装置(S)を設け、 前記膜分離槽(E2)底部に沈殿する沈殿汚泥を前記汚
泥貯留槽(N2)に返送する沈殿汚泥移送管(A4)を
設け、 前記汚泥貯留槽(N2)上部に被処理水を濾過する濾過
膜装置(C1)を内装するとともに、前記汚泥貯留槽
(N2)から汚泥貯留槽(N2)に隣接する他の槽に前
記濾過膜装置(C1)で濾過済の濾過水を移送する濾過
水移送管(A6)を設けて、前記濾過膜装置(C1)に
連設してある浄化槽。2. A sludge storage tank (N2) and a membrane separation tank (E).
2) and a purification tank provided with another tank adjacent to the sludge storage tank (N2) , wherein a solid obtained by solid-liquid separation of the water to be treated from the other tank is provided.
Screen filtration for transferring material to the sludge storage tank (N2)
An apparatus (S) is provided, and the settled sludge settled at the bottom of the membrane separation tank (E2) is treated with the sludge.
Settling sludge transfer pipe (A4) returned to mud storage tank (N2)
And a filtration membrane device (C1) for filtering the water to be treated is provided above the sludge storage tank (N2), and the sludge storage tank (N2) is provided in another tank adjacent to the sludge storage tank (N2). A purification tank provided with a filtered water transfer pipe (A6) for transferring filtered water filtered by the filtration membrane device (C1), and connected to the filtration membrane device (C1).
2)および汚泥貯留槽(N2)に隣接する他の槽を設け
た浄化槽であって、 前記他の槽からの被処理水を固液分離してえられた固形
物を前記汚泥貯留槽 (N2)に移送するスクリーン濾過
装置(S)を設け、 前記膜分離槽(E2)底部に沈殿する沈殿汚泥を前記汚
泥貯留槽(N2)に返送する沈殿汚泥移送管(A4)を
設け、 前記汚泥貯留槽(N2)上部に被処理水を濾過する濾過
膜装置(C1)を内装するとともに、前記汚泥貯留槽
(N2)から汚泥貯留槽(N2)に隣接する他の槽に前
記濾過膜装置(C1)で濾過済の濾過水を移送する濾過
水移送管(A6)を設けて、前記濾過膜装置(C1)に
連設し、 前記汚泥貯留槽(N2)の水位を、前記他の槽の水位よ
りも高く設定し、 前記被処理水移送管(A6)を、前記汚泥貯留槽(N
2)の水位以下に設けるとともに、 前記濾過膜装置(C1)の下方に散気管(D1)を設
け、前記濾過膜装置(C1)の下方に供給される被処理
水を固液分離するスクリーン(C3)を設け、 前記スクリーン(C3)の下方には、前記スクリーン
(C3)に気泡を供給する散気装置(D2)を設け てあ
る浄化槽。3. A sludge storage tank (N2) and a membrane separation tank (E).
2) and a purification tank provided with another tank adjacent to the sludge storage tank (N2) , wherein a solid obtained by solid-liquid separation of the water to be treated from the other tank is provided.
Screen filtration for transferring material to the sludge storage tank (N2)
An apparatus (S) is provided, and the settled sludge settled at the bottom of the membrane separation tank (E2) is treated with the sludge.
Settling sludge transfer pipe (A4) returned to mud storage tank (N2)
And a filtration membrane device (C1) for filtering the water to be treated is provided above the sludge storage tank (N2), and the sludge storage tank (N2) is provided in another tank adjacent to the sludge storage tank (N2). A filtration water transfer pipe (A6) for transferring filtered water filtered by the filtration membrane device (C1) is provided, connected to the filtration membrane device (C1), and the water level of the sludge storage tank (N2) is set to the level. The water level of the other tanks
And the treated water transfer pipe (A6) is connected to the sludge storage tank (N
A water diffuser (D1) is installed below the filtration membrane device (C1) while being provided below the water level of 2).
The processing target supplied below the filtration membrane device (C1)
A screen (C3) for solid-liquid separation of water is provided, and the screen (C3) is provided below the screen (C3).
A septic tank provided with a diffuser (D2) for supplying air bubbles to (C3) .
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP29505795A JP3271882B2 (en) | 1995-11-14 | 1995-11-14 | Septic tank |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP29505795A JP3271882B2 (en) | 1995-11-14 | 1995-11-14 | Septic tank |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH09136096A JPH09136096A (en) | 1997-05-27 |
JP3271882B2 true JP3271882B2 (en) | 2002-04-08 |
Family
ID=17815764
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP29505795A Expired - Lifetime JP3271882B2 (en) | 1995-11-14 | 1995-11-14 | Septic tank |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3271882B2 (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002205087A (en) * | 2001-01-09 | 2002-07-23 | Kubota Corp | Air diffuser |
JP2003024959A (en) * | 2001-07-17 | 2003-01-28 | Fuji Clean Kogyo Kk | Method and apparatus for treating wastewater |
JP5079285B2 (en) * | 2006-08-31 | 2012-11-21 | 株式会社ハウステック | Wastewater septic tank |
JP5651384B2 (en) * | 2010-06-18 | 2015-01-14 | 株式会社クボタ | Sewage treatment equipment, sewage treatment method, and method for renovating sewage treatment equipment |
-
1995
- 1995-11-14 JP JP29505795A patent/JP3271882B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPH09136096A (en) | 1997-05-27 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP5651384B2 (en) | Sewage treatment equipment, sewage treatment method, and method for renovating sewage treatment equipment | |
JP5048708B2 (en) | Septic tank | |
JP3271882B2 (en) | Septic tank | |
JP3469797B2 (en) | Sewage treatment method and apparatus | |
JP3561460B2 (en) | Livestock wastewater sewage treatment method and apparatus | |
KR200189492Y1 (en) | The inclined precipitation tank in waste water disposal plant by microorganism contact | |
JP4090218B2 (en) | Sewage treatment apparatus and operation method thereof | |
JP2003010871A (en) | Sewage treatment apparatus and its operating method | |
KR100288980B1 (en) | Method for Biological Filter Beds for Sewage and Wastewater Treatment | |
JP3716461B2 (en) | Concentration method in the receiving tank for biological filtration backwash wastewater | |
JP4865997B2 (en) | Operation method of sewage treatment apparatus and sewage treatment apparatus | |
JP4405130B2 (en) | Two floor juxtaposed aerobic treatment tank and sewage septic tank with steps | |
KR950011768B1 (en) | Sewage purification facility by anaerobic and aerobic contact circulation method and treatment method | |
JPH0639391A (en) | Method for treating waste water | |
JP3759288B2 (en) | Wastewater septic tank | |
JP2905072B2 (en) | Sewage treatment system | |
KR100458908B1 (en) | Dirty and waste water purifying system | |
JP3288560B2 (en) | Membrane separation tank and septic tank | |
JPH06190384A (en) | Apparatus and method for purifying sewage | |
JP2831066B2 (en) | Small merger processing septic tank | |
JP2000084579A (en) | Sewage treatment equipment | |
JPH10156375A (en) | Biological filter and sewage septic tank containing the filter | |
JP2000197892A (en) | Purification tank and its operation method | |
KR200235045Y1 (en) | Waste water disposal plant having sheet filter in FRP | |
KR200308803Y1 (en) | Dirty and waste water purifying system |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20090125 Year of fee payment: 7 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20090125 Year of fee payment: 7 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20100125 Year of fee payment: 8 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20100125 Year of fee payment: 8 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20110125 Year of fee payment: 9 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20110125 Year of fee payment: 9 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20120125 Year of fee payment: 10 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20120125 Year of fee payment: 10 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20130125 Year of fee payment: 11 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20140125 Year of fee payment: 12 |
|
EXPY | Cancellation because of completion of term |