JP3167530B2 - Septic tank - Google Patents

Septic tank

Info

Publication number
JP3167530B2
JP3167530B2 JP09462794A JP9462794A JP3167530B2 JP 3167530 B2 JP3167530 B2 JP 3167530B2 JP 09462794 A JP09462794 A JP 09462794A JP 9462794 A JP9462794 A JP 9462794A JP 3167530 B2 JP3167530 B2 JP 3167530B2
Authority
JP
Japan
Prior art keywords
tank
treated
water
activated sludge
treatment tank
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 - Fee Related
Application number
JP09462794A
Other languages
Japanese (ja)
Other versions
JPH07299485A (en
Inventor
八郎 佐藤
良人 北井
和之 本田
正修 岩橋
勝己 浜田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kubota Corp
Original Assignee
Kubota Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Kubota Corp filed Critical Kubota Corp
Priority to JP09462794A priority Critical patent/JP3167530B2/en
Publication of JPH07299485A publication Critical patent/JPH07299485A/en
Application granted granted Critical
Publication of JP3167530B2 publication Critical patent/JP3167530B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、被処理水の原水の流入
口側から一次処理槽、活性汚泥処理槽を順に設けた浄化
槽に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a purification tank provided with a primary treatment tank and an activated sludge treatment tank in this order from the inlet side of raw water to be treated.

【0002】[0002]

【従来の技術】通常、この種の浄化槽は、活性汚泥処理
槽における被処理水の収容深さを、一次処理槽における
被処理水の収容深さと同じ大きさに形成してあり、一般
的には内径の等しい筒形状の浄化槽本体内を仕切って前
記活性汚泥処理槽と一次処理槽とを形成していた。
2. Description of the Related Art Generally, in this type of septic tank, the depth of the water to be treated in the activated sludge treatment tank is formed to be the same as the depth of the water to be treated in the primary treatment tank. Has divided the inside of a cylindrical septic tank body having the same inner diameter to form the activated sludge treatment tank and the primary treatment tank.

【0003】また、活性汚泥処理槽に代表される、好気
性菌による生物処理を行う好気槽には、大量の酸素を供
給する必要性があり、通常は、その好気槽内にエア供給
する散気管を設け、その好気槽内に酸素を供給する構成
にしてあったものの、その好気槽内の被処理水に酸素を
効率よく溶解させるには、被処理水の収容深さを大きく
取ることが有利であると考えられている。また、活性汚
泥処理槽に膜分離装置を内装してなる膜分離槽を設けて
ある場合には、濾過面積の大きな膜分離装置を内装する
ためにも、前記活性汚泥処理槽の被処理水の収容深さを
深くすることが望まれており、いずれにしても前記活性
汚泥処理槽の被処理水収容深さを深くすることが望まれ
ている。そこで、浄化槽を全体として一次処理槽と活性
汚泥処理槽との両方ともに深く設計し、前記活性汚泥処
理槽の被処理水収容深さを深くすることが考えられてい
る。
[0003] In addition, an aerobic tank, such as an activated sludge treatment tank, for performing biological treatment with aerobic bacteria needs to supply a large amount of oxygen. Usually, air is supplied into the aerobic tank. Although it was configured to supply oxygen into the aerobic tank, a dispersing tube was provided to increase the depth of the water to be treated. It is considered advantageous to take large amounts. When the activated sludge treatment tank is provided with a membrane separation tank having a membrane separation device installed therein, in order to install a membrane separation device having a large filtration area, the water to be treated in the activated sludge treatment tank is provided. It is desired to increase the accommodation depth, and in any case, it is desired to increase the treatment water accommodation depth of the activated sludge treatment tank. Therefore, it has been considered that both the primary treatment tank and the activated sludge treatment tank are designed deeply as a whole to increase the depth of the activated sludge treatment tank to accommodate the water to be treated.

【0004】[0004]

【発明が解決しようとする課題】ところが、浄化槽は一
般に埋設して用いられるものの、上述のように浄化槽全
体を単に深く設計した場合には、その浄化槽を埋設する
浄化槽埋設用の穴を大きく掘削しなければならず、埋設
作業に伴う土木工事が困難になるとともに、その土木工
事費が高くなるという欠点があり、埋設作業を行う点か
らは、浄化槽全体を浅く形成することが望まれていた。
However, although the septic tank is generally buried and used, if the entire septic tank is simply designed deep as described above, a large hole for burying the septic tank for embedding the septic tank is excavated. However, there is a drawback that civil engineering work associated with the burial work becomes difficult and the cost of the civil engineering work increases. From the viewpoint of the burial work, it has been desired that the entire septic tank be formed shallow.

【0005】この事は、先に述べた活性汚泥処理槽への
酸素供給効率や、濾過効率を向上させたいという処理効
率の向上を目的とする要望と相反するものであり、これ
らの要望を両立させることは困難であった。
This conflicts with the above-mentioned demand for improving the efficiency of supplying oxygen to the activated sludge treatment tank and the efficiency of processing to improve the efficiency of filtration. It was difficult to do.

【0006】従って、本発明の目的は、上記実情に鑑
み、埋設作業に支障をきたすことなく、活性汚泥処理槽
内での被処理水の処理効率を、向上出来る浄化槽を提供
することにある。
Accordingly, an object of the present invention is to provide a purification tank capable of improving the treatment efficiency of the water to be treated in the activated sludge treatment tank without hindering the burying work in view of the above-mentioned circumstances.

【0007】[0007]

【課題を解決するための手段】この目的を達成するため
の本発明の第一特徴構成は、被処理水の原水の流入口側
から一次処理槽、活性汚泥処理槽を順に設けた浄化槽に
おいて、前記活性汚泥処理槽における被処理水の収容深
さを、前記一次処理槽における被処理水の収容深さより
も大に形成し、前記活性汚泥処理槽に、脱窒素槽と、膜
分離装置を内装した膜分離槽とを設けるとともに、被処
理水が前記脱窒素槽から前記膜分離槽へ自然移流自在に
構成し、前記膜分離槽内の被処理水を前記脱窒素槽に返
送する被処理水返送手段を設けてあることにあり、上記
第一特徴構成において、前記一次処理槽が、被処理水を
濾過する生物濾過槽もしくは嫌気濾床槽を含むものであ
り、その生物濾過槽内で濾過した被処理水もしくは前記
嫌気濾床槽からの被処理水を前記活性汚泥処理槽へ移流
させる移流機構を設けてあるものであってもよく、前記
一次処理槽が、流量調整槽を含むものであり、前記流量
調整槽には、その流量調整槽から前記活性汚泥処理槽へ
定量的に被処理水を移流させる移流機構を設けてあって
よい。 又、この目的を達成するための本発明の第二特
徴構成は、被処理水の原水の流入口側から一次処理槽、
活性汚泥処理槽を順に設けた浄化槽において、前記活性
汚泥処理槽における被処理水の収容深さを、前記一次処
理槽における被処理水の収容深さよりも大に形成し、
記一次処理槽に脱窒素槽を設けるとともに、前記活性汚
泥処理槽を、膜分離装置を内装してなる膜分離槽から構
成し、被処理水が、前記脱窒素槽から膜分離槽へ自然移
流自在に構成し、前記膜分離槽内の被処理水を、前記脱
窒素槽へ返送する被処理水返送手段を設けてあることに
ある。 そして、上記構成による作用効果は以下の通りで
ある。
A first feature of the present invention to achieve this object is a purification tank provided with a primary treatment tank and an activated sludge treatment tank in this order from the inlet side of raw water to be treated. The storage depth of the water to be treated in the activated sludge treatment tank is formed larger than the storage depth of the water to be treated in the primary treatment tank , and the activated sludge treatment tank has a denitrification tank and a membrane.
A membrane separation tank equipped with a separation device is provided.
Natural flow of natural water from the denitrification tank to the membrane separation tank
And the water to be treated in the membrane separation tank is returned to the denitrification tank.
There that is provided with a treatment water return means for feeding, the
In the first characteristic configuration, the primary treatment tank includes a biological filtration tank or an anaerobic filter bed tank for filtering water to be treated, and the water to be treated or the anaerobic filter bed tank filtered in the biological filtration tank is used. May be provided with an advection mechanism for advancing the water to be treated to the activated sludge treatment tank , wherein the primary treatment tank includes a flow rate adjustment tank, and the flow rate adjustment tank has a flow rate adjustment tank. An advection mechanism for quantitatively advancing the water to be treated from the adjusting tank to the activated sludge treatment tank may be provided . The second feature of the present invention for achieving this object is as follows.
The feature composition is the primary treatment tank from the inlet side of the raw water to be treated,
In a septic tank provided with an activated sludge treatment tank in order,
The storage depth of the water to be treated in the sludge treatment tank
Formed to be larger than the depth of the water to be treated in the treatment tank, and provided with a denitrification tank in the primary treatment tank, and the activated sludge treatment tank was constituted by a membrane separation tank equipped with a membrane separation device, The water to be treated is configured so that it can freely flow from the denitrification tank to the membrane separation tank, and the water to be treated in the membrane separation tank is provided with a treated water return means for returning the water to the denitrification tank.
is there. The operation and effect of the above configuration are as follows.

【0008】[0008]

【作用】つまり、活性汚泥処理槽における被処理水の収
容深さを、前記一次処理槽における被処理水の収容深さ
よりも大に形成してあることで、浄化槽全体を深く形成
することなく、前記活性汚泥処理槽のみを従来よりも深
く形成して浄化槽を構成することが出来、これにより、
前記活性汚泥処理槽へエア供給する場合には、被処理水
中の深い位置から散気することが出来る。その活性汚泥
処理槽に供給された気泡は、深い位置から水面までの長
い経路を通って移動するので、気泡と被処理水とが十分
に接触するとともに、深い位置では、気泡にかかる水圧
が高く酸素の溶解効率が高いため、気泡から被処理水へ
の酸素溶解が良好に行われるようになる。また、前記活
性汚泥処理槽が、膜分離装置を内装してなる膜分離槽を
含んでなる場合には、上述の深い位置からの散気による
気泡により、被処理水が槽内を上昇する上昇流速の速い
位置に前記膜分離装置を配置することが出来、被処理水
の流速の速い位置に膜分離装置を配置する事で、前記膜
分離装置の膜表面を効率よく洗浄する効果が得られ、膜
面の目詰まりを抑制することもできる。
In other words, the storage depth of the water to be treated in the activated sludge treatment tank is formed larger than the storage depth of the water to be treated in the primary treatment tank, so that the entire septic tank is not formed deep. Only the activated sludge treatment tank can be formed deeper than before to constitute a purification tank, whereby
When supplying air to the activated sludge treatment tank, air can be diffused from a deep position in the water to be treated. Since the bubbles supplied to the activated sludge treatment tank move along a long path from a deep position to the surface of the water, the bubbles and the water to be treated sufficiently come into contact with each other. Since the oxygen dissolving efficiency is high, the oxygen can be satisfactorily dissolved from the bubbles into the water to be treated. Further, in the case where the activated sludge treatment tank includes a membrane separation tank in which a membrane separation device is installed, the water to be treated rises in the tank due to the bubbles generated by the aeration from the deep position. The membrane separation device can be arranged at a position where the flow rate is fast, and by arranging the membrane separation device at a position where the flow rate of the water to be treated is fast, the effect of efficiently cleaning the membrane surface of the membrane separation device can be obtained. Also, clogging of the film surface can be suppressed.

【0009】さらに、前記活性汚泥処理槽に、脱窒素槽
と、膜分離装置を内装した膜分離槽とを設けるととも
に、被処理水が前記脱窒素槽から前記膜分離槽へ自然移
流自在に構成し、前記膜分離槽内の被処理水を前記脱窒
素槽に返送する被処理水返送手段を設けてあれば、高負
荷な被処理水であっても前記膜分離槽で酸素供給を十分
に行って被処理水の硝化(アンモニア性窒素を硝酸性窒
素に変換する生物処理)を行え、さらに、前記脱窒素槽
内を比較的酸素供給量の少ない条件に維持できるので、
その硝化済の被処理水は、脱窒素槽内で脱窒(硝酸性窒
素を窒素ガスに変換する生物処理)作用が良好に進行
し、被処理水は高度に浄化された状態になり、被処理水
の処理能力を向上させることが出来るという利点があ
る。また、膜分離装置を内装してなる膜分離槽を採用す
ることにより、活性汚泥処理槽は、小型に形成でき、大
きな縦穴を形成せずとも浄化槽の埋設作業を行え、埋設
作業を簡単に行うことが出来るようになる。
Further, a denitrification tank is provided in the activated sludge treatment tank.
And a membrane separation tank equipped with a membrane separation device.
The water to be treated is naturally transferred from the denitrification tank to the membrane separation tank.
It is configured to flow freely, and the water to be treated in the membrane separation tank is denitrified.
If there is a means for returning treated water to be returned to the tank,
Oxygen supply is sufficient in the membrane separation tank even for heavy water to be treated.
And nitrification of the water to be treated
Biological treatment for conversion to nitrogen)
The interior can be maintained under relatively low oxygen supply conditions,
The nitrified water to be treated is denitrified in a denitrification tank (nitrate nitrate).
Biological treatment that converts nitrogen into nitrogen gas)
The treated water becomes highly purified and the treated water
Has the advantage that the processing capacity of
You. In addition, a membrane separation tank equipped with a membrane separation device is adopted.
In this way, the activated sludge treatment tank can be formed small and large.
Septic tanks can be buried without forming vertical holes
Work can be done easily.

【0010】また、前記一次処理槽が、被処理水を濾過
する生物濾過槽もしくは嫌気濾床槽を含むものであり、
その生物濾過槽内で濾過した被処理水や、前記嫌気濾床
槽を経た被処理水を前記活性汚泥処理槽へ移流させる移
流機構を設けてあるものであれば、前記活性汚泥処理槽
には、前記生物濾過槽での生物濾過、もしくは、前記嫌
気濾床槽での嫌気処理により固形物の除去された被処理
水が移流することになり、活性汚泥処理槽内での被処理
水の処理性能(活性)が低下しにくい。
[0010] Further , the primary treatment tank filters the water to be treated.
Including a biological filtration tank or an anaerobic filter bed tank,
The water to be treated filtered in the biological filtration tank or the anaerobic filter bed
Transfer of the water to be treated that has passed through the tank to the activated sludge treatment tank.
If the flow mechanism is provided, the activated sludge treatment tank
The biological filtration in the biological filtration tank, or
Solids removed by anaerobic treatment in the filter bed tank
Water will be advected and will be treated in the activated sludge treatment tank.
Water treatment performance (activity) does not easily decrease.

【0011】また、前記一次処理槽が、流量調整槽を含
むものであり、前記流量調整槽には、その流量調整槽か
ら前記活性汚泥処理槽へ定量的に被処理水を移流させる
移流機構を設けてあれば、前記活性汚泥処理槽へは定量
的に被処理水が移流するので、活性汚泥処理槽内の水質
は一定に保たれ易く、前記活性汚泥処理槽で定常的に被
処理水の処理を行っても、前記活性汚泥処理槽内の水質
を低下させずに、被処理水の好気処理が安定に行える。
Further , the primary treatment tank includes a flow control tank.
The flow control tank is provided with the flow control tank.
To quantitatively transfer the water to be treated to the activated sludge treatment tank
If an advection mechanism is provided, a fixed amount can be supplied to the activated sludge treatment tank.
Water in the activated sludge treatment tank
Is easily maintained at a constant level, and is constantly covered in the activated sludge treatment tank.
Even if the treated water is treated, the water quality in the activated sludge treatment tank
The aerobic treatment of the water to be treated can be performed stably without lowering the water content.

【0012】[0012]

【発明の効果】従って、浄化槽全体を深く形成する場合
には、浄化槽を埋設するのに深い穴を形成せねばなら
ず、埋設作業に多大な労力を要して困難になるのに対
し、作業性をあまり低下させることなく、浄化槽を埋設
することが出来るようになり、かつ、被処理水の処理効
率を向上できたので、処理済の処理済液は十分に浄化さ
れたものになりやすく、放出される処理済の被処理水の
水質を向上させることが出来、水質汚染などの環境汚染
を低減するのに役立ち、あまり費用をかけずに低公害を
実現するのに有利になった。
Therefore, when the entire septic tank is formed deeply, a deep hole must be formed to bury the septic tank, which requires a great deal of labor for embedding. The septic tank can be buried without significantly lowering the properties, and the treatment efficiency of the water to be treated has been improved, so that the treated liquid that has been treated is likely to be sufficiently purified, The quality of the discharged treated water to be treated can be improved, which helps to reduce environmental pollution such as water pollution, and is advantageous for achieving low pollution at a low cost.

【0013】また、活性汚泥処理槽の活性が低下しにく
い構成に出来るので、長期にわたって安定に浄化槽を用
いることが出来るようにもなる。
[0013] Further, since the activated sludge treatment tank can be made to have a structure in which the activity is hardly reduced, the purification tank can be used stably for a long period of time.

【0014】[0014]

【実施例】以下に本発明の実施例を図面に基づいて説明
する。
Embodiments of the present invention will be described below with reference to the drawings.

【0015】図1に示すように、本発明の浄化槽は、被
処理水の原水の流入口I側から一次処理槽1、活性汚泥
処理槽2をそれぞれ別の容器で構成し、被処理水がこの
順に移流するように連通管Jで連結して設けてあり、前
記一次処理槽1は、沈殿分離槽N1と、生物濾過槽B1
とから構成してあり、前記活性汚泥処理槽2は、脱窒素
槽N2と、膜分離槽Eとから構成してある。
As shown in FIG. 1, the septic tank according to the present invention comprises a primary treatment tank 1 and an activated sludge treatment tank 2 which are separate from the inlet I of raw water to be treated. The primary treatment tank 1 is provided with a sedimentation separation tank N1 and a biological filtration tank B1 so as to be connected by a communication pipe J so as to flow in this order.
The activated sludge treatment tank 2 is composed of a denitrification tank N2 and a membrane separation tank E.

【0016】前記一次処理槽1は、高さが約1.4mの
容器の内部空間を二室に仕切って、被処理水の収容深さ
約1.2mの沈殿分離槽N1と生物濾過槽B1とを形成
してある。前記沈殿分離槽N1は、一次処理槽1へ流入
した被処理水の原水を受け、その被処理水を一時貯留
し、原水中に含まれる夾雑物を沈殿分離するとともに、
内部に生息する嫌気性菌により、前記被処理水を嫌気分
解させる構成にしてある。前記生物濾過槽B1は、好気
濾床Cを内装するとともに、その好気濾床Cの下方には
その好気濾床Cに対してエア供給する散気管D1を設け
てあり、好気濾床C内を通過する被処理水を好気分解し
て汚泥の少ない状態に処理可能である。さらに、前記生
物濾過槽B1にはU字管Uを立設してあり、そのU字管
Uは前記生物濾過槽B1内の前記好気濾床Cの上部に一
端を開口させ、前記好気濾床Cを通過した生物濾過済の
被処理水を、取り入れ自在に構成し、他端には移流管A
1を連設し、U字管Uの底部にブロワからエア供給する
ことで、エアリフト作用により前記生物濾過槽B1内の
被処理水を、U字管U及び、移流管A1を介して活性汚
泥処理槽2へ移流させられる移流機構Aを構成してあ
る。尚、前記移流管A1は、前記一次処理槽1と、前記
活性汚泥処理槽2との内部を連通する連通管Jに接続さ
れているものとし、被処理水は前記連通管Jを通じて前
記一次処理槽1から前記活性汚泥処理槽2へ移流するも
のであり、前記連通管Jには、逆流を防止する逆止弁V
を設けてあり、前記活性汚泥処理槽2内の活性汚泥(浮
遊汚泥に多数の好気性菌が密生したもの)が逆流するな
どして濃度が低下することがおきにくい構成にしてあ
り、前記活性汚泥処理槽2内の活性を高く維持し易く、
かつ、活性汚泥が前記生物濾過槽B1に逆流して好気濾
床Cが目詰まりし易くなるのを防止する構成にしてあ
る。
The primary treatment tank 1 divides an inner space of a container having a height of about 1.4 m into two chambers, and a sedimentation separation tank N1 and a biological filtration tank B1 having an accommodation depth of about 1.2 m. Is formed. The sedimentation separation tank N1 receives the raw water to be treated that has flowed into the primary treatment tank 1, temporarily stores the water to be treated, and precipitates and separates impurities contained in the raw water,
The water to be treated is anaerobically decomposed by anaerobic bacteria living inside. The biological filtration tank B1 is adapted to interior aerobic filter bed C, the lower the aerobic filter bed C is provided with a diffusion pipe D1 to the air supply for its aerobic filter bed C, Koki濾The water to be treated passing through the floor C can be aerobicly decomposed and treated in a state where sludge is small. Further, a U-shaped pipe U is erected on the biological filtration tank B1, and the U-shaped pipe U is opened at one end above the aerobic filter bed C in the biological filtration tank B1, and the aerobic The biologically filtered water to be treated that has passed through the filter bed C is configured to be freely taken in, and the other end of the advection tube A
1 and the air to be supplied from the blower to the bottom of the U-shaped pipe U, the water to be treated in the biological filtration tank B1 is activated sludge through the U-shaped pipe U and the advection pipe A1 by an air lift action. An advection mechanism A for advancing to the processing tank 2 is configured. The advection pipe A1 is connected to a communication pipe J that communicates between the primary treatment tank 1 and the activated sludge treatment tank 2, and the water to be treated is subjected to the primary treatment through the communication pipe J. A flow is transferred from the tank 1 to the activated sludge treatment tank 2. The communication pipe J has a check valve V for preventing backflow.
The activated sludge in the activated sludge treatment tank 2 (the sludge in which a large number of aerobic bacteria are densely packed in the suspended sludge) flows back and the like, so that the concentration is hardly reduced. It is easy to keep the activity in the sludge treatment tank 2 high,
In addition, the configuration is such that the activated sludge is prevented from flowing back into the biological filtration tank B1 to easily clog the aerobic filter bed C.

【0017】前記活性汚泥処理槽2は、高さが約1.8
mの容器の内部空間を二室に仕切って、被処理水の収容
深さ約1.4mの脱窒素槽N2と膜分離槽Eとを形成し
てある。前記脱窒素槽N2は、前記生物濾過槽B1から
流入した被処理水を受けて一時貯留するように構成する
とともに、内部には循環ポンプP1を配して、前記脱窒
素槽N2内の被処理水を常時循環させられる構成にして
ある。前記膜分離槽Eは、高濃度の活性汚泥を収容し、
被処理水に含まれる高濃度のBODを生物処理可能に構
成してあるとともに、平膜の多数を並設して構成してあ
る膜分離装置Mを内装してある。前記膜分離装置Mの下
方には、気泡を供給して、平膜表面に汚泥等が付着する
のを防止する散気管D2を設けてあり、散気操作するこ
とで膜分離槽E内の好気性菌に酸素を供給し、かつ、前
記平膜の表面を洗浄可能に構成し、平膜の膜分離処理性
能を高く維持できるようにしてある。前記平膜には、前
記平膜から被処理水を吸引濾過して放流するための放流
ポンプP2を連設して、高度に浄水された被処理水を取
出自在に構成してある。また、前記膜分離槽内にはエア
リフトポンプA2を立設して、ブロワからのエア供給に
より、前記膜分離槽E内の被処理水を、前記脱窒素槽N
2へ返送自在に設けてある。
The activated sludge treatment tank 2 has a height of about 1.8.
The interior space of the m container is divided into two chambers to form a denitrification tank N2 and a membrane separation tank E having a depth of about 1.4 m for the water to be treated. The denitrification tank N2 is configured to receive and temporarily store the water to be treated that has flowed from the biological filtration tank B1, and a circulation pump P1 is disposed inside the denitrification tank N2. It is configured to constantly circulate water. The membrane separation tank E contains a high concentration of activated sludge,
A high-concentration BOD contained in the water to be treated is configured to be biologically treatable, and a membrane separation device M configured by arranging a large number of flat membranes in parallel is provided therein. A diffuser D2 is provided below the membrane separator M to supply air bubbles to prevent sludge and the like from adhering to the flat membrane surface. Oxygen is supplied to the aerial bacteria, and the surface of the flat membrane is configured to be washable so that the membrane separation treatment performance of the flat membrane can be maintained at a high level. A discharge pump P2 for suction-filtering and discharging the water to be treated from the flat membrane and discharging the same is connected to the flat membrane so that highly purified water to be treated can be taken out. Further, an air lift pump A2 is erected in the membrane separation tank, and water to be treated in the membrane separation tank E is supplied to the denitrification tank N by air supply from a blower.
2 is provided so as to be freely returned.

【0018】このような構成の浄化槽に被処理水を流入
させると、一次処理槽1に流入した被処理水の原水は、
沈殿分離槽N1で夾雑物を除去されつつ嫌気処理が行わ
れ、嫌気処理の済んだ被処理水は、自然移流して下部か
ら前記生物濾過槽B1に流入する。生物濾過槽B1に流
入した被処理水は生物濾過を受けつつ上昇し、汚泥混入
の少ない状態で前記U字管Uに流入する。U字管Uに流
入した被処理水は、移流機構Aを経て脱窒素槽N2に流
入し、脱窒素槽N2内の活性汚泥により分解を受けつつ
膜分離槽Eへ移流する。その膜分離槽Eに流入した被処
理水は、散気管D2からのエア供給により、好気分解を
受けて硝化されつつ、再度前記脱窒素槽N2に返送され
たり、膜分離装置Mで濾過されたりする。返送された被
処理水は、前記脱窒素槽N2が前記膜分離槽Eよりもや
や嫌気気味になっているために、脱窒作用が良好に行わ
れ、被処理水が高度に浄化されたものになり、さらに活
性汚泥処理槽2内で循環される被処理水の水質が向上す
る。従って、前記膜分離槽E内の膜分離装置Mから濾過
される被処理水の水質が向上するとともに、膜分離装置
Mにより、汚泥の混入のほとんどない処理済液が得られ
るので浄化槽から放流される水質は高度に浄化されたも
のとなる。
When the water to be treated flows into the septic tank having such a structure, the raw water to be treated flowing into the primary treatment tank 1
Anaerobic treatment is performed while impurities are removed in the sedimentation separation tank N1, and the water to be treated after the anaerobic treatment flows naturally and flows into the biological filtration tank B1 from below. The water to be treated that has flowed into the biological filtration tank B1 rises while being subjected to biological filtration, and flows into the U-shaped pipe U in a state where there is little mixing of sludge. The water to be treated that has flowed into the U-shaped pipe U flows into the denitrification tank N2 via the advection mechanism A, and flows to the membrane separation tank E while being decomposed by the activated sludge in the denitrification tank N2. The water to be treated, which has flowed into the membrane separation tank E, is returned to the denitrification tank N2 again or filtered by the membrane separation device M while undergoing aerobic decomposition and nitrification by air supply from the diffuser D2. Or The returned to-be-processed water is one in which the denitrification action is favorably performed and the to-be-treated water is highly purified because the denitrification tank N2 is slightly more anaerobic than the membrane separation tank E. And the quality of the water to be circulated in the activated sludge treatment tank 2 is further improved. Therefore, the quality of the water to be treated, which is filtered from the membrane separation device M in the membrane separation tank E, is improved, and the membrane separation device M provides a treated liquid with almost no mixing of sludge. Water quality will be highly purified.

【0019】このような浄化槽を設置する場合には、地
上から掘削して形成すべき浄化槽埋設用の縦穴を従来の
土木工事で形成していた大きさよりも一部のみ大に形成
するだけで設置でき、設置するのに必要な労力をあまり
増やすことなく処理能力の高い浄化槽を設置出来た。
When such a septic tank is installed, the vertical hole for burying the septic tank to be formed by excavating from the ground is formed only partially larger than the size formed by the conventional civil engineering work. It was possible to install a septic tank with a high treatment capacity without increasing the labor required for installation.

【0020】〔別実施例〕以下に別実施例を説明する。
先の実施例の一次処理槽1にかえて次のような構成の一
次処理槽1を用いてもよい。図2に示す一次処理槽1
は、内部空間を二室に仕切って、沈殿分離槽N1と流量
調整槽B2とを形成してある。前記流量調整槽B2は、
被処理水中に含まれる固形物を破砕もしくは分離して主
に流動性の高い液状物を通過させるスクリーンSを内装
するとともに、そのスクリーンSに気泡を供給して、そ
のスクリーンSに引っかかった固形物をさらに分解する
散気管D3を内装してある。また、前記流量調整槽B2
内の被処理水を定量的に汲み上げる移流ポンプP3を内
装し、固形物をあまり含まない被処理水を定量的に活性
汚泥処理槽2へ移送可能な移流機構Aを構成してある。
このような構成によれば、たとえ一次処理槽1に大量の
被処理水の原水が流入したとしても、活性汚泥処理槽2
では定常的な被処理水の処理を行え、前記活性汚泥処理
槽2内の水質を低下させずに、常に安定した水質の処理
済液を放流することが出来るようになる。
[Another embodiment] Another embodiment will be described below.
The primary processing tank 1 having the following configuration may be used in place of the primary processing tank 1 in the above embodiment. Primary treatment tank 1 shown in FIG.
Has an inner space divided into two chambers, and a sedimentation separation tank N1 and a flow rate adjustment tank B2 are formed. The flow rate adjusting tank B2 is
A screen S that crushes or separates solids contained in the water to be treated and passes mainly a liquid having a high fluidity is installed, and air bubbles are supplied to the screen S, and solids trapped on the screen S are provided. Is further provided therein. In addition, the flow control tank B2
An advection pump P3 for quantitatively pumping the water to be treated therein is provided therein, and constitutes an advection mechanism A capable of quantitatively transferring the water to be treated containing little solid matter to the activated sludge treatment tank 2.
According to such a configuration, even if a large amount of raw water flows into the primary treatment tank 1, the activated sludge treatment tank 2
In this manner, the water to be treated can be constantly treated, and the treated liquid having a stable water quality can always be discharged without lowering the water quality in the activated sludge treatment tank 2.

【0021】さらに、一次処理槽1には、前記生物濾過
槽に代えて、嫌気濾床を内装してなる嫌気濾床槽や、好
気性菌を育成する好気濾床を内装するとともに、好気濾
床の下方に散気管を内装してなる好気濾床槽、もしく
は、被処理水中の汚泥を沈殿させ、固形物の含有量を減
少させる沈殿槽等を含むものであってもよく、原水中に
含まれる固形物が大まかに処理され、活性汚泥処理槽に
移流する被処理水中に固形物が含まれにくい構成であれ
ば好ましく、固形物の流入により、活性汚泥処理槽内の
被処理水処理能力が低下するような事態が起きにくく、
長期にわたって安定に使用することが出来る。また、前
記沈殿分離槽に代えて、嫌気濾床槽を用いる等の構成の
変更を行っても良い。
Further, in the primary treatment tank 1, instead of the biological filtration tank, an anaerobic filter tank containing an anaerobic filter bed or an aerobic filter bed for growing aerobic bacteria is provided. An aerobic filter bed tank equipped with an air diffuser below the air filter bed, or a sedimentation tank that precipitates sludge in the water to be treated and reduces the content of solids may be included. It is preferable that the solid matter contained in the raw water is roughly treated, and the solid matter is hardly contained in the treated water flowing to the activated sludge treatment tank. It is unlikely that water treatment capacity will decrease,
It can be used stably for a long time. Further, the configuration may be changed such as using an anaerobic filter bed tank instead of the precipitation separation tank.

【0022】また、前記活性汚泥処理槽2についても、
内部を二槽に仕切って構成する例を示したが、一槽のみ
からなる活性汚泥処理槽2であってもよく、この場合、
活性汚泥処理槽2は、膜分離装置Mを内装してなる膜分
離槽Eから構成してあることが望ましく、膜分離槽Eを
採用することで安定した被処理水処理を行うことが出
来、処理済液の水質を高く維持できる。さらに、このよ
うな場合、脱窒素槽を一次処理槽に形成してあることが
望ましく、前記一次処理槽に脱窒素槽を設けるととも
に、前記活性汚泥処理槽を、膜分離装置を内装してなる
膜分離槽から構成し、被処理水が、前記脱窒素槽から膜
分離槽へ自然移流自在に構成し、前記膜分離槽内の被処
理水を、前記脱窒素槽へ返送する被処理水返送手段を設
けてあれば、先の実施例と同様に、高度に被処理水を浄
水する事が出来るようになる。
Further, the activated sludge treatment tank 2 also includes:
Although the example in which the interior is divided into two tanks is shown, the activated sludge treatment tank 2 may be composed of only one tank.
The activated sludge treatment tank 2 is desirably constituted by a membrane separation tank E in which a membrane separation device M is installed, and by employing the membrane separation tank E, stable treatment of the water to be treated can be performed. The water quality of the treated liquid can be kept high. Further, in such a case, it is preferable that the denitrification tank is formed in the primary treatment tank, and the primary treatment tank is provided with a denitrification tank, and the activated sludge treatment tank is equipped with a membrane separation device. A membrane separation tank, the water to be treated is configured to freely flow from the denitrification tank to the membrane separation tank, and the water to be treated in the membrane separation tank is returned to the denitrification tank. If the means is provided, the water to be treated can be highly purified as in the previous embodiment.

【0023】また、前記一次処理槽1と、活性汚泥処理
槽2とは、別の容器で形成することなく一体のものであ
ってもよい。さらに、その大きさについても、先の実施
例に示したものに限らず、様々な形態に設計可能であ
る。
Further, the primary treatment tank 1 and the activated sludge treatment tank 2 may be integrated without being formed in separate containers. Further, the size is not limited to that shown in the above embodiment, and can be designed in various forms.

【0024】さらに、前記膜分離装置Mは、下部のみな
らず、深さ方向にわたって全長に設けてあってもよく、
具体的には、膜分離装置Mを2段に重ねて設けてあって
もよい。また、上部のみに設けてあってもよい。
Further, the membrane separation device M may be provided not only at the lower part but also over the entire length in the depth direction.
Specifically, the membrane separation devices M may be provided in two stages. Also, it may be provided only on the upper part.

【0025】また、前記一次処理槽1から活性汚泥処理
槽2へ被処理水を移流させる移流機構Aは、定量的、も
しくは、固形物を除去した状態で、被処理水を移流させ
るものに限らず、単純に被処理水を移流させるだけの簡
単な構成にしてあってもよい。
The advection mechanism A for advancing the water to be treated from the primary treatment tank 1 to the activated sludge treatment tank 2 is not limited to a mechanism for advancing the water to be treated quantitatively or in a state in which solids are removed. Instead, it may have a simple configuration in which the water to be treated is simply advected.

【0026】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 accompanying drawings.

【図面の簡単な説明】[Brief description of the drawings]

【図1】実施例における浄化槽の縦断側面図FIG. 1 is a vertical sectional side view of a septic tank in an embodiment.

【図2】別実施例における浄化槽の縦断側面図FIG. 2 is a vertical sectional side view of a septic tank in another embodiment.

【符号の説明】[Explanation of symbols]

I 流入管 1 一次処理槽 2 活性汚泥処理槽 B1 生物濾過槽 B2 流量調整槽 E 膜分離槽 M 膜分離装置 N2 脱窒素槽 A2 被処理水返送手段 I Inflow pipe 1 Primary treatment tank 2 Activated sludge treatment tank B1 Biological filtration tank B2 Flow control tank E Membrane separation tank M Membrane separation device N2 Denitrification tank A2 Treated water return means

フロントページの続き (51)Int.Cl.7 識別記号 FI C02F 3/34 101 C02F 3/34 101B (72)発明者 岩橋 正修 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 (56)参考文献 実願 平1−147526号(実開 平3− 86094号)の願書に添付した明細書及び 図面の内容を撮影したマイクロフィルム (JP,U) 実願 平3−12704号(実開 平4− 99291号)の願書に添付した明細書及び 図面の内容を撮影したマイクロフィルム (JP,U) 「し尿浄化槽ハンドブック」大野茂 監 (昭56年11月26日)産業用水調査会 p120〜125、p238〜241、p268 (58)調査した分野(Int.Cl.7,DB名) C02F 3/12 C02F 3/00 Continued on the front page (51) Int.Cl. 7 Identification symbol FI C02F 3/34 101 C02F 3/34 101B (72) Inventor Masaharu Iwahashi 2 in Takamatsu, Kosai-cho, Koga-gun, Shiga Prefecture Inside Kubota Shiga Plant Co., Ltd. (72) Inventor Katsumi Hamada 2nd Takamatsu, Kosai-cho, Koga-gun, Shiga Prefecture Inside the Kubota Shiga Plant, Inc. (56) References Attached to the application form Japanese Utility Model Application No. 1-147526 (Japanese Utility Model Application No. 3-86094). Microfilm (JP, U) photographing the contents of the specification and drawings attached The microfilm (JP, U) photographing the contents of the specifications and drawings attached to the application for Japanese Utility Model Application No. Hei 3-12704 (Japanese Utility Model Application No. Hei 4-99291) JP, U) "Sewage Septic Tank Handbook" by Shigeru Ohno (November 26, 1956) Industrial Water Research Committee p120-125, p238-241, p268 (58) Fields surveyed (Int. Cl. 7 , DB name) C02F 3/12 C02F 3/00

Claims (5)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 被処理水の原水の流入口(I)側から一
次処理槽(1)、活性汚泥処理槽(2)を順に設けた浄
化槽であって、 前記活性汚泥処理槽(2)における被処理水の収容深さ
を、前記一次処理槽(1)における被処理水の収容深さ
よりも大に形成し 前記活性汚泥処理槽(2)に、脱窒素槽(N2)と、膜
分離装置(M)を内装した膜分離槽(E)とを設けると
ともに、被処理水が前記脱窒素槽(N2)から前記膜分
離槽(E)へ自然移流自在に構成し、前記膜分離槽
(E)内の被処理水を前記脱窒素槽(N2)に返送する
被処理水返送手段(A2)を設けてある 浄化槽。
1. A purifying tank provided with a primary treatment tank (1) and an activated sludge treatment tank (2) in this order from the inlet (I) side of raw water to be treated, wherein the activated sludge treatment tank (2) The storage depth of the water to be treated is formed larger than the storage depth of the water to be treated in the primary treatment tank (1) , and the activated sludge treatment tank (2) is provided with a denitrification tank (N2) and a membrane.
When a membrane separation tank (E) containing a separation device (M) is installed,
In both cases, the water to be treated is removed from the denitrification tank (N2)
The separation tank (E) is configured to be freely advected naturally, and the membrane separation tank
Return the water to be treated in (E) to the denitrification tank (N2)
A septic tank provided with a treated water return means (A2) .
【請求項2】 前記一次処理槽(1)が、被処理水を濾
過する生物濾過槽(B1)を含むものであり、その生物
濾過槽(B1)内で濾過した被処理水を前記活性汚泥処
理槽(2)へ移流させる移流機構を設けてある請求項1
に記載の浄化槽。
2. The primary treatment tank (1) includes a biological filtration tank (B1) for filtering water to be treated, and the water to be treated filtered in the biological filtration tank (B1) is treated with the activated sludge. An advection mechanism for advancing to the processing tank (2) is provided.
The septic tank described in 1.
【請求項3】 前記一次処理槽(1)が、被処理水を濾
過する嫌気濾床槽を含むものであり、その嫌気濾床槽か
らの被処理水を前記活性汚泥処理槽(2)へ移流させる
移流機構を設けてある請求項1〜2のいずれかに記載の
浄化槽。
3. The primary treatment tank (1) includes an anaerobic filter tank for filtering water to be treated, and the water to be treated from the anaerobic filter tank is supplied to the activated sludge treatment tank (2). The septic tank according to claim 1, further comprising an advection mechanism for advection.
【請求項4】 前記一次処理槽(1)が、流量調整槽
(B2)を含むものであり、前記流量調整槽(B2)に
は、その流量調整槽(B2)から前記活性汚泥処理槽
(2)へ定量的に被処理水を移流させる移流機構を設け
てある請求項1〜3のいずれかに記載の浄化槽。
4. The primary treatment tank (1) includes a flow rate adjusting tank (B2), and the flow rate adjusting tank (B2) is provided with the activated sludge treatment tank (B) from the flow rate adjusting tank (B2). The septic tank according to any one of claims 1 to 3, further comprising an advection mechanism for quantitatively advancing the water to be treated to 2).
【請求項5】 被処理水の原水の流入口(I)側から一
次処理槽(1)、活性汚泥処理槽(2)を順に設けた浄
化槽であって、 前記活性汚泥処理槽(2)における被処理水の収容深さ
を、前記一次処理槽(1)における被処理水の収容深さ
よりも大に形成し、 前記一次処理槽(1)に脱窒素槽(N2)を設けるとと
もに、前記活性汚泥処理槽(2)を、膜分離装置(M)
を内装してなる膜分離槽(E)から構成し、被処理水
が、前記脱窒素槽(N2)から膜分離槽(E)へ自然移
流自在に構成し、前記膜分離槽(E)内の被処理水を、
前記脱窒素槽(N2)へ返送する被処理水 返送手段(A
2)を設けてある 浄化槽。
5. A method according to claim 1, wherein the raw water is treated in one direction from an inlet (I) side of the raw water.
Purification with the next treatment tank (1) and activated sludge treatment tank (2)
And the depth of storage of the water to be treated in the activated sludge treatment tank (2).
Is the storage depth of the water to be treated in the primary treatment tank (1).
When the primary treatment tank (1) is provided with a denitrification tank (N2)
In addition, the activated sludge treatment tank (2) is connected to a membrane separation device (M).
And a membrane separation tank (E) containing
Is naturally transferred from the denitrification tank (N2) to the membrane separation tank (E).
It is configured to flow freely, and the water to be treated in the membrane separation tank (E) is
Means for returning treated water (A ) to be returned to the denitrification tank (N2)
A septic tank provided with 2) .
JP09462794A 1994-05-09 1994-05-09 Septic tank Expired - Fee Related JP3167530B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP09462794A JP3167530B2 (en) 1994-05-09 1994-05-09 Septic tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP09462794A JP3167530B2 (en) 1994-05-09 1994-05-09 Septic tank

Publications (2)

Publication Number Publication Date
JPH07299485A JPH07299485A (en) 1995-11-14
JP3167530B2 true JP3167530B2 (en) 2001-05-21

Family

ID=14115505

Family Applications (1)

Application Number Title Priority Date Filing Date
JP09462794A Expired - Fee Related JP3167530B2 (en) 1994-05-09 1994-05-09 Septic tank

Country Status (1)

Country Link
JP (1) JP3167530B2 (en)

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
「し尿浄化槽ハンドブック」大野茂 監 (昭56年11月26日)産業用水調査会 p120〜125、p238〜241、p268

Also Published As

Publication number Publication date
JPH07299485A (en) 1995-11-14

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