JPH06320181A - Sludge transfer device for combined treating septic tank - Google Patents

Sludge transfer device for combined treating septic tank

Info

Publication number
JPH06320181A
JPH06320181A JP11052193A JP11052193A JPH06320181A JP H06320181 A JPH06320181 A JP H06320181A JP 11052193 A JP11052193 A JP 11052193A JP 11052193 A JP11052193 A JP 11052193A JP H06320181 A JPH06320181 A JP H06320181A
Authority
JP
Japan
Prior art keywords
tank
pipe
treated water
anaerobic filter
contact aeration
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP11052193A
Other languages
Japanese (ja)
Inventor
Seiichiro Nakamoto
政一郎 仲本
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.)
Sekisui Chemical Co Ltd
Original Assignee
Sekisui Chemical Co Ltd
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 Sekisui Chemical Co Ltd filed Critical Sekisui Chemical Co Ltd
Priority to JP11052193A priority Critical patent/JPH06320181A/en
Publication of JPH06320181A publication Critical patent/JPH06320181A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To provide a sludge transfer device, for combined treating septic tank, which prevents pulsation of the water being transferred and can easily adjust the amt. of sludge transferred with a relatively simple structure and which is easy to maintain and inspect. CONSTITUTION:A branch pipe 21 is connected to the upper end of a water lifting pipe 16 leading to a contact aeration tank to provide a division into two branching directions and a pipe arrangement is made in such a manner that the end of one branch is positioned at the upper part of a first chamber of an anaerobic filter bed tank and the end of the other branch is positioned at the interior upper part of the contact aeration tank. An opening part 27a is formed on the upper side of an intermediate part of a first pipe 22 leading from the branch pipe to the upper part of the first chamber of the anaerobic filter bed tank, a rising part 27b is provided in the pipe below the opening part to suppress pulsation of the water being transferred for treatment and a flow meter 27c with V-shaped notch part is provided to measure the amt. of the water flowing over the rising part and toward the first chamber of the anaerobic filter bed tank.

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、家庭の台所、浴室、洗
面所等から排出される生活雑排水と、水洗トイレから排
出されるし尿とを併せて処理する合併処理浄化槽の汚泥
移送装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a sludge transfer device for a combined treatment septic tank for treating domestic wastewater discharged from a kitchen, bathroom, washroom, etc. of a home and human waste discharged from a flush toilet. .

【0002】[0002]

【従来の技術】家庭から排出される生活雑排水やし尿
は、川や湖沼等を汚染する大きな原因とであると言われ
ている。そのような生活排水による川や湖沼等の汚染を
未然に防止する目的で家庭に設置される小型浄化槽とし
て、水洗トイレから排出されるし尿のみを単独に処理す
る単独処理浄化槽と、し尿と生活雑排水の両方を併せて
処理する合併処理浄化槽とがあるが、河川等の汚染防止
の観点からは後者の合併処理浄化槽の設置が好ましい。
2. Description of the Related Art Domestic wastewater and night soil discharged from homes are said to be a major cause of pollution of rivers and lakes. As a small septic tank installed at home for the purpose of preventing pollution of rivers and lakes due to such domestic wastewater, a single septic tank that treats only human excrement discharged from flush toilets separately, and human waste and household waste. There is a combined treatment septic tank that treats both wastewater together, but the latter combined treatment septic tank is preferable from the viewpoint of preventing pollution of rivers and the like.

【0003】この合併処理浄化槽にも、例えば嫌気ろ床
接触ばっ気方式によるものや、分離接触ばっ気方式によ
るものなど各種のタイプがあるが、ここでは、一例とし
て嫌気ろ床接触ばっ気方式によるものについて説明す
る。
There are various types of combined treatment septic tanks, such as those using the anaerobic filter bed contact aeration method and those using the separation contact aeration method. Here, as an example, the anaerobic filter bed contact aeration method is used. Describe things.

【0004】これは、相対向する壁面上部に流入管およ
び流出管がそれぞれ接続される浄化槽本体を有し、この
本体内を上流側(流入管側)から下流側(流出管側)に
向けて順番に壁で仕切って複数の処理槽を形成するとと
もに、それらの処理槽を処理水が順次通過するように各
仕切り壁の所定位置に開口部を形成して隣合う処理槽を
連通させたものである。
This has a septic tank main body to which an inflow pipe and an outflow pipe are connected, respectively, in the upper part of the opposite wall surfaces, and the inside of this main body is directed from the upstream side (inflow pipe side) to the downstream side (outflow pipe side). A plurality of treatment tanks are formed by sequentially partitioning with walls, and an opening is formed at a predetermined position of each partition wall so that the treated water can pass through these treatment tanks in sequence so that adjacent treatment tanks communicate with each other. Is.

【0005】各処理槽は、上流側に位置するものから順
番に嫌気ろ床槽(その上流側に沈殿分離槽が設けられる
場合もある)、接触ばっ気槽、沈殿槽と呼ばれており、
嫌気ろ床槽には、嫌気性微生物が表面に付着するろ材
が、また接触ばっ気槽には、好気性微生物が表面に付着
する接触材と、外部の送風機から接触ばっ気槽内にエア
を供給する散気管とが、さらに沈殿槽には上部に消毒槽
がそれぞれ設けられる。そして、流入管を介して浄化槽
本体内に導入された汚水を、まず嫌気ろ床槽で嫌気処理
し、次いで接触ばっ気槽でばっ気処理して浄化し、さら
に沈殿槽で剥離汚泥を沈殿させて上澄み液と分離させ、
その上澄み液を消毒槽で消毒した上で流出管を介して外
部に放流するようになっている。
Each treatment tank is called an anaerobic filter bed tank (a precipitation separation tank may be provided on the upstream side in some cases), a contact aeration tank, and a precipitation tank in order from the one located upstream.
The anaerobic filter tank has a filter material on which anaerobic microorganisms adhere to the surface, and the contact aeration tank has a contact material on which aerobic microorganisms adhere to the surface, and air is blown into the contact aeration tank from an external blower. A supply air diffuser and a disinfection tank are provided above the settling tank. Then, the sewage introduced into the main body of the septic tank through the inflow pipe is first anaerobically treated in the anaerobic filter bed tank, and then aerated in the contact aeration tank to purify it, and then the separated sludge is settled in the sedimentation tank. Separate from the supernatant,
The supernatant liquid is disinfected in a disinfection tank and then discharged to the outside through an outflow pipe.

【0006】このような合併処理浄化槽おいては、使用
期間が長くなると接触ばっ気槽の接触材表面の付着汚泥
(生物膜)が肥厚化して、接触材中の流路が目詰まりを
起こし、その結果、生物膜と槽内水との接触効率が低下
して処理性能が落ちる。そのため、これを回復する目的
で定期的(例えば6か月に一度の割合)に逆洗作業が行
われる。これは、接触材の底部に設けられた逆洗管と呼
ばれる散気装置(逆洗装置)から気泡を発散させて接触
材表面から汚泥を剥離させ、この剥離汚泥を、揚水管と
これにエアを供給するエア量調整バルブ付の送気管とで
なるエアリフトポンプで汲み上げて汚泥移送管を通じて
嫌気ろ床槽へ移送するものである。
In such a combined treatment septic tank, the sludge (biological film) adhering to the surface of the contact material of the contact aeration tank thickens when the use period becomes long, and the flow path in the contact material becomes clogged. As a result, the contact efficiency between the biofilm and the water in the tank is reduced and the treatment performance is deteriorated. Therefore, the backwashing work is performed regularly (for example, once every 6 months) for the purpose of recovering it. This is because air bubbles are emitted from an air diffuser (backwashing device) called a backwash pipe provided at the bottom of the contact material to separate the sludge from the surface of the contact material. It is pumped up by an air lift pump consisting of an air supply pipe with an air amount adjusting valve for supplying air and transferred to an anaerobic filter tank through a sludge transfer pipe.

【0007】また、最近では、水質性能をさらに向上さ
せるため、上記エアリフトポンプや汚泥移送管を使用
し、接触ばっ気槽内の汚泥を含む処理水を一定の割合で
嫌気ろ床槽に移送して常時循環させることが提唱されて
いる。これは、接触ばっ気槽内で有機物中の窒素分を酸
化して亜硝酸化又は硝酸化した後、それらを嫌気ろ床槽
に移送して槽内の脱窒細菌の作用でガス状の窒素
(N2 )に変換して飛散させようというものである。こ
れによれば、リンと同時に湖沼等における藻類等の発生
要因で飲料水の悪臭原因ともなっている窒素分を除去す
ることができ、同時にBOD(生化学的酸素要求量)源
の除去も可能となる。
Further, recently, in order to further improve the water quality performance, the above-mentioned air lift pump and sludge transfer pipe are used to transfer the treated water containing sludge in the contact aeration tank to the anaerobic filter tank at a constant ratio. It is advocated to always circulate it. This is because the nitrogen content in the organic matter is oxidized in the contact aeration tank to nitrite or nitrify it, and then they are transferred to an anaerobic filter bed tank, where they are converted into gaseous nitrogen by the action of denitrifying bacteria. It is intended to be converted to (N 2 ) and scattered. According to this, it is possible to remove not only phosphorus but also nitrogen content which is a cause of malodor in drinking water due to factors such as algae in lakes and the like, and at the same time, removal of BOD (biochemical oxygen demand) source. Become.

【0008】ところで、接触ばっ気槽から嫌気ろ床槽又
は沈殿分離槽(以下、ここでは単に嫌気ろ床槽という)
に移送すべき汚泥を含む処理水の量、つまり汚泥移送量
については、逆洗時には多く循環時には少なくなるよう
に必要に応じて適切に調整する必要がある。しかし、上
述したように揚水管内に供給されるエアのリフト作用に
より汚泥を含む処理水を汲み上げて汚泥移送管を通じて
嫌気ろ床槽へと移送されることから、移送管内を流れる
移送水には絶えず脈動が伴うこととなり、そのままでは
移送水量が一定しないために適切な水量調整を行いにく
いという問題がある。
By the way, from the contact aeration tank to the anaerobic filter bed tank or the precipitation separation tank (hereinafter, simply referred to as anaerobic filter bed tank)
The amount of treated water containing sludge to be transferred to, that is, the amount of sludge transferred needs to be appropriately adjusted as necessary so that it is large during backwash and small during circulation. However, as described above, since the treated water containing sludge is pumped up by the lift action of the air supplied to the pumping pipe and is transferred to the anaerobic filter tank through the sludge transfer pipe, the transfer water flowing in the transfer pipe is constantly Since pulsation is involved, the amount of transferred water is not constant as it is, and it is difficult to properly adjust the amount of water.

【0009】そこで、このような問題に対処するため、
従来の合併処理浄化槽においては、例えば特開平4−7
1688号公報や実開平3−86097号公報に示され
ているように、汚泥移送経路の途中に移送水量(汚泥移
送量)の調整手段が設けられることがある。
Therefore, in order to deal with such a problem,
In a conventional combined treatment septic tank, for example, Japanese Patent Laid-Open No. 4-7
As disclosed in Japanese Patent No. 1688 and Japanese Utility Model Laid-Open No. 3-86097, a means for adjusting a transfer water amount (sludge transfer amount) may be provided in the middle of the sludge transfer route.

【0010】このうち、前者の公報に記載されたもの
は、エアリフトポンプを構成する揚水管の上部に四角形
の箱状の計量装置を配置し、その内部に2枚の板状の堰
を間隔をあけて平行に且つ着脱可能に設けて、その堰の
上部に計量部となるV状の切り欠きを形成した構成で、
揚水管によって計量装置内に汲み上げられた汚泥を含む
処理水のうち一部が一方の堰を越えて沈殿分離槽に移送
され、他の一部が他方の堰を越えて沈殿槽上部の浄化槽
に移送され、残りがポンプ槽に戻されるようにしたもの
である。これによれば、揚水管を通じ汲み上げられた処
理水が計量装置を通過する際に、その脈動が或る程度抑
えられるとともに、必要に応じて計量装置内の堰を取り
替えることで移送水の調整も可能となる。
Among them, the one disclosed in the former publication has a rectangular box-shaped metering device arranged on the upper part of a pumping pipe which constitutes an air lift pump, and two plate-like weirs are arranged inside the metering device. With a structure in which the weir is provided in parallel and detachably, and a V-shaped notch serving as a measuring unit is formed on the upper part of the weir,
Part of the treated water containing sludge pumped up into the metering device by the pumping pipe is transferred to the sedimentation separation tank over one weir, and the other part is transferred to the septic tank above the sedimentation tank over the other weir. It is transferred and the rest is returned to the pump tank. According to this, when the treated water pumped through the pumping pipe passes through the metering device, its pulsation is suppressed to some extent, and the transfer water can be adjusted by replacing the weir in the metering device as necessary. It will be possible.

【0011】また、後者の公報に記載されたものは、揚
水管の上部に気液分離室を形成し、この気液分離室内の
液流出部側に堰と整流用バッフルとを取り付け、かつ気
液分離室の液流出部と反対側に、処理水の水位を一定に
保つ切り欠きを設けたものである。これによれば、接触
ばっ気槽から気液分離室内に汲み上げられた処理水のう
ち一定水位を越えた分は上記切り欠きを介して接触ばっ
気槽に戻され、その残りの処理水が流出管を通じて嫌気
ろ床槽に移送されるが、その際、移送される処理水が上
記バッフルおよび堰を越えるようになっていることで、
その脈動が或る程度は抑制されることになる。
In the latter publication, the gas-liquid separation chamber is formed in the upper part of the pumping pipe, the weir and the rectifying baffle are attached to the liquid outflow side of the gas-liquid separation chamber, and the gas is separated. A notch for keeping the water level of the treated water constant is provided on the opposite side of the liquid outflow portion of the liquid separation chamber. According to this, of the treated water pumped from the contact aeration tank into the gas-liquid separation chamber, the portion exceeding a certain water level is returned to the contact aeration tank through the notch, and the remaining treated water flows out. It is transferred to the anaerobic filter tank through a pipe, but at that time, the transferred treated water passes over the baffle and the weir,
The pulsation will be suppressed to some extent.

【0012】[0012]

【発明が解決しようとする課題】しかし、前者の公報記
載の構成によると、揚水管の上部に比較的大きな箱状の
計量装置を設けるため、それに見合った大きな設置スペ
ースが必要となる。その場合、揚水管の上方に十分な空
きスペースがあれば問題はないが、実際は、浄化槽本体
のマンホールからの点検作業等が容易に行えるようにす
るために揚水管の上方周辺には、各種の配管、バルブ、
計器類等が集まっていることが多い。従って、あまり大
きな設置スペースを確保するのは困難であり、設置でき
たとしても他の配管のバルブ操作や保守点検等が行いに
くくなるという問題がある。
However, according to the structure described in the former publication, since a relatively large box-shaped measuring device is provided above the pumping pipe, a large installation space commensurate with it is required. In that case, there is no problem as long as there is a sufficient empty space above the pumping pipe, but in actuality, in order to facilitate inspection work from the manhole of the septic tank main body, there are various Piping, valves,
In many cases, instruments are gathered. Therefore, it is difficult to secure an excessively large installation space, and even if the installation space can be installed, there is a problem that it becomes difficult to perform valve operation and maintenance inspection of other piping.

【0013】一方、後者の公報に記載されたものは、前
者のものに比べると構造が簡単で保守点検も容易である
かもしれないが、揚水管の直上方の気液分離室内に整流
用バッフルと堰とが配置されているため、気液分離室内
の水位が脈動によって変動した時にその脈動が十分吸収
される前に比較的容易に処理水が堰を乗り越えてしまう
とともに、その流出管側には流量計が存在しないため、
流量調整も行いにくいという問題がある。
On the other hand, the latter publication may have a simpler structure and easier maintenance and inspection than the former one, but the baffle for rectification is provided in the gas-liquid separation chamber just above the pumping pipe. Since the water and the weir are arranged, when the water level in the gas-liquid separation chamber fluctuates due to pulsation, the treated water relatively easily crosses over the weir before the pulsation is sufficiently absorbed, and at the outflow pipe side. Because there is no flow meter,
There is a problem that it is difficult to adjust the flow rate.

【0014】本発明は、従来の合併処理浄化槽における
上記のような問題に対処するもので、接触ばっ気槽から
嫌気ろ床槽又は沈殿分離槽に移送される汚泥を含む処理
水(移送水)の脈動を防止して汚泥移送量ないし移送水
量を容易に調整できるとともに、小さな設置スペースで
足り、しかも保守点検や管理を容易に行える簡素な構造
の合併処理浄化槽の汚泥移送装置を提供することを目的
とする。
The present invention addresses the above-mentioned problems in the conventional combined treatment septic tank, and the treated water containing sludge (transfer water) transferred from the contact aeration tank to the anaerobic filter bed tank or the precipitation separation tank. To provide a sludge transfer device for a combined treatment septic tank with a simple structure that can prevent the pulsation of the sludge and easily adjust the sludge transfer amount or the transfer water amount, requires a small installation space, and can easily perform maintenance inspection and management. To aim.

【0015】[0015]

【課題を解決するための手段】上記目的達成のため、本
発明に係る汚泥移送装置は、流入する汚水を嫌気処理す
る嫌気ろ床槽又は沈殿分離処理する沈殿分離槽と、その
嫌気又は沈殿分離処理された処理水を好気処理する接触
ばっ気槽と、この接触ばっ気槽内の処理水を揚水する揚
水管と、この揚水管の下部に一端が接続されて送風機か
らのエアを揚水管内に供給する送気管と、この送気管を
介して揚水管内に供給されるエアの量を調整するエア量
調整バルブとを有し、上記揚水管により接触ばっ気槽内
の汚泥を含む処理水の一部を揚水して嫌気ろ床槽又は沈
殿分離槽に移送するようにした合併処理浄化槽におい
て、次のように構成したことを特徴とする。
To achieve the above object, a sludge transfer device according to the present invention comprises an anaerobic filter bed tank for anaerobic treatment of inflowing sewage or a sedimentation separation tank for sedimentation separation treatment, and its anaerobic or sedimentation separation. A contact aeration tank for aerobically treating the treated water, a pumping pipe for pumping the treated water in the contact aeration tank, and one end connected to the lower part of the pumping pipe to draw air from the blower inside the pumping pipe. And an air amount adjusting valve for adjusting the amount of air supplied into the pumping pipe through this pipe, and the treated water containing sludge in the aeration tank contacted by the pumping pipe. A combined treatment septic tank in which a part of the pumped water is transferred to an anaerobic filter tank or a precipitation separation tank is characterized by having the following configuration.

【0016】すなわち、上記揚水管の上端部に分岐管を
接続して2方向に分岐させ、その分岐された一方の端部
が嫌気ろ床槽又は沈殿分離処理槽の上部に、他方の端部
が接触ばっ気槽内の上部にそれぞれ位置するように配管
する。そして、上記分岐管から嫌気ろ床槽又は沈殿分離
層の上部に到る配管の途中の管上部側に開口部を形成
し、この開口部の下方の管内に、移送される処理水の脈
動を抑制する堰と、この堰を越えて嫌気ろ床槽又は沈殿
分離層の方に流れる処理水の流量を計測するV状の切り
欠き部を有する流量計とを設ける。
That is, a branch pipe is connected to the upper end of the pumping pipe to branch in two directions, and one end of the branch is on the upper side of the anaerobic filter bed or the precipitation separation treatment tank, and the other end. Are located in the upper part of the contact aeration tank. Then, an opening is formed on the upper side of the pipe in the middle of the pipe from the branch pipe to the upper part of the anaerobic filter bed or the precipitation separation layer, and the pulsation of the treated water to be transferred into the pipe below the opening. A suppressing weir and a flow meter having a V-shaped notch for measuring the flow rate of the treated water flowing over the weir toward the anaerobic filter bed or the precipitation separation layer are provided.

【0017】[0017]

【作用】このように構成された合併処理浄化槽の汚泥移
送装置において、接触ばっ気槽から嫌気ろ床槽又は沈殿
分離槽への汚泥ないし処理水の移送量は、次のようにし
て調整される。
In the sludge transfer device of the combined treatment septic tank configured as described above, the transfer amount of sludge or treated water from the contact aeration tank to the anaerobic filter bed tank or sedimentation separation tank is adjusted as follows. .

【0018】まず、接触ばっ気槽に設けられた揚水管の
下部に送気管を介して送風機からエアが供給されると、
供給されたエアの気泡分だけ揚水管内の処理水の比重が
軽くなり、その水位が接触ばっ気槽の水位よりも高くな
る。このようなエアリフト作用は、揚水管に供給される
エア量を多くすればするほど顕著となるから、送気管の
エア量調整バルブによって揚水管による揚水量を調整す
ることができる。
First, when air is supplied from the blower to the lower part of the pumping pipe provided in the contact aeration tank through the air blower,
The specific gravity of the treated water in the pumping pipe becomes lighter by the amount of bubbles of the supplied air, and the water level becomes higher than the water level in the contact aeration tank. Since such an air lift action becomes more remarkable as the amount of air supplied to the pumping pipe is increased, the pumping amount of the pumping pipe can be adjusted by the air amount adjusting valve of the air supply pipe.

【0019】次に、こうして接触ばっ気槽の水位以上に
汲み上げられた汚泥を含む処理水は、揚水管の上部に接
続された分岐管を介して2方向に分岐され、さらにその
分岐管に接続された配管を通じて、一部は接触ばっ気槽
の上部に導かれた上で必要に応じて接触ばっ気槽内に戻
され、他の一部は嫌気ろ床槽又は沈殿分離槽の上部に導
かれる。
Next, the treated water containing the sludge pumped up above the water level in the contact aeration tank is branched into two directions via a branch pipe connected to the upper part of the pumping pipe, and further connected to the branch pipe. Part of the gas is introduced to the upper part of the contact aeration tank through the piping provided and then returned to the contact aeration tank as needed, and the other part is introduced to the upper part of the anaerobic filter bed tank or sedimentation separation tank. Get burned.

【0020】従って、逆洗の時には、接触ばっ気槽の上
部に到る配管の端部を蓋等により閉鎖して接触ばっ気槽
に処理水が戻らないようにしておくことにより、揚水管
を通じて汲み上げられた汚泥を含む処理水の全てが嫌気
ろ床槽又は沈殿分離槽に移送されることになる。
Therefore, at the time of backwashing, the end of the pipe reaching the upper part of the contact aeration tank is closed by a lid or the like to prevent the treated water from returning to the contact aeration tank, so that the pumping pipe is All of the treated water including the sludge that has been pumped up will be transferred to the anaerobic filter bed tank or sedimentation tank.

【0021】一方、循環時には、揚水管を通じて汲み上
げられた汚泥を含む処理水の一部を接触ばっ気槽の上部
に到る配管の端部から接触ばっ気槽に戻すようにしてお
くことにより、上記処理水のうちの一定量が嫌気ろ床槽
又は沈殿分離槽に移送されることになる。
On the other hand, during circulation, a part of the treated water containing sludge pumped up through the pumping pipe is returned to the contact aeration tank from the end of the pipe reaching the upper part of the contact aeration tank. A certain amount of the treated water is transferred to the anaerobic filter bed tank or the precipitation separation tank.

【0022】その場合、本発明の構成においては、分岐
管から嫌気ろ床槽又は沈殿分離層の上部に到る配管の途
中の管上部側に開口部が形成され且つその開口部の下方
の管内に堰とV状の切り欠きを有する流量計とが設けら
れているので、分岐管側から嫌気ろ床槽又は沈殿分離槽
へと移送される処理水つまり移送水は、まず、その堰に
一旦当たることにより、脈動が抑制されると同時に勢い
が或る程度弱められる。その結果、堰を越えて下流側に
流れる移送水は、比較的脈動の少ない定常流に近いもの
となる。
In that case, in the structure of the present invention, an opening is formed on the upper side of the pipe in the middle of the pipe from the branch pipe to the upper part of the anaerobic filter bed or the precipitation separation layer, and inside the pipe below the opening. Since a weir and a flow meter having a V-shaped notch are provided in the, the treated water transferred from the branch pipe side to the anaerobic filter tank or the sedimentation separation tank, that is, the transfer water, first flows to the weir once. By hitting, the pulsation is suppressed and at the same time the momentum is weakened to some extent. As a result, the transfer water flowing downstream beyond the weir becomes a steady flow with relatively few pulsations.

【0023】そして、この定常流に近い移送水が流量計
を通過して最終的に嫌気ろ床槽又は沈殿分離槽に移送さ
れるが、その際、流量計は開口部の下方に配置されてい
るから、外部から目視によって移送水の通過量、つまり
移送水量を容易に知ることができる。従って、こうして
計測された移送水量に基づいて、例えば上記エア調整バ
ルブにより揚水量を加減するなどすることにより、嫌気
ろ床槽等に移送すべき汚泥ないし処理水の量を容易に調
整することができる。
Then, the transfer water close to this steady flow passes through the flow meter and is finally transferred to the anaerobic filter tank or the sedimentation separation tank. At that time, the flow meter is arranged below the opening. Therefore, the passing amount of the transferred water, that is, the transferred water amount can be easily known from the outside. Therefore, based on the transfer water amount measured in this way, the amount of sludge or treated water to be transferred to the anaerobic filter tank or the like can be easily adjusted by, for example, adjusting the pumping amount with the air adjustment valve. it can.

【0024】[0024]

【実施例】以下、本発明の実施例について説明する。図
1および図2は、本実施例における合併処理浄化槽の全
体構成を示す概略平面図および縦断面図である。
EXAMPLES Examples of the present invention will be described below. 1 and 2 are a schematic plan view and a vertical sectional view showing the overall configuration of the combined treatment septic tank in this embodiment.

【0025】これらの図に示すように、合併処理浄化槽
1は、相対向する上流側(図面上、左側)および下流側
(図面上、右側)の壁面の上部に流入管2および流出管
3がそれぞれ接続された浄化槽本体4を有する。
As shown in these drawings, in the combined treatment septic tank 1, an inflow pipe 2 and an outflow pipe 3 are provided at the upper portions of the upstream (left side in the drawing) and downstream (right side in the drawing) wall surfaces facing each other. Each has a septic tank body 4 connected thereto.

【0026】浄化槽本体4内は、その上部を除く部分
が、上流側から下流側に向けて順番に設けられた第1、
第2および第3仕切り壁4a、4b、4cによって、嫌
気ろ床槽第1室5、嫌気ろ床槽第2室6、接触ばっ気槽
7、沈殿槽8に区画されている。そして、第1仕切り壁
4aの上部に設けられた連通口4a’を介して嫌気ろ床
槽第1室5と第2室6とが連通され、第2仕切り壁4b
の上部に設けられた連通口4bを介して嫌気ろ床槽第2
室6と接触ばっ気槽7とが連通され、さらに第3仕切り
壁4cの下部に設けられた連通部4c’を介して接触ば
っ気槽7と沈殿槽8とが連通されている。
The inside of the septic tank main body 4 except the upper portion is provided in order from the upstream side to the downstream side.
The anaerobic filter bed first chamber 5, the anaerobic filter bed second chamber 6, the contact aeration tank 7, and the precipitation tank 8 are partitioned by the second and third partition walls 4a, 4b, and 4c. Then, the anaerobic filter bed first chamber 5 and the second chamber 6 are communicated with each other through a communication port 4a ′ provided on the upper part of the first partition wall 4a, and the second partition wall 4b.
The anaerobic filter bed second through the communication port 4b provided in the upper part of the
The chamber 6 and the contact aeration tank 7 are communicated with each other, and the contact aeration tank 7 and the settling tank 8 are communicated with each other via a communication portion 4c ′ provided under the third partition wall 4c.

【0027】嫌気ろ床槽第1室5および第2室6には、
それぞれ、表面に嫌気性微生物が形成されるろ材9、1
0が設けられているとともに、処理水の流路および清掃
孔を兼ねた角筒状の筒部5a、6aが第1仕切り壁4a
および第2仕切り壁4bに沿って形成されている。そし
て、流入管2を通じて第1室5に流入した汚水が、同室
内のろ材9を通過する際にその表面に生成された嫌気性
微生物によって嫌気処理された後、第1仕切り壁4a側
の筒部5aおよび連通口4a’を通って第2室6に流入
し、さらにこの第2室6でも同室内のろ材10により再
び嫌気処理が行われた上で、第2仕切り壁4b’側の筒
部6aおよび連通口4b’を通って接触ばっ気槽7側に
流入するようになっている。
In the anaerobic filter bed first chamber 5 and the second chamber 6,
Filter media 9, 1 on the surface of which anaerobic microorganisms are formed, respectively
No. 0 is provided, and the tubular portions 5a and 6a of the rectangular tubular shape that also serve as the flow path of the treated water and the cleaning hole are the first partition wall 4a.
And it is formed along the 2nd partition wall 4b. Then, the sewage that has flowed into the first chamber 5 through the inflow pipe 2 is anaerobically treated by the anaerobic microorganisms generated on the surface of the filter medium 9 in the same chamber, and then the first partition wall 4a side cylinder. After flowing into the second chamber 6 through the portion 5a and the communication port 4a ', the anaerobic treatment is performed again in the second chamber 6 by the filter medium 10 in the same chamber, and then the cylinder on the second partition wall 4b' side. It is adapted to flow into the contact aeration tank 7 side through the portion 6a and the communication port 4b '.

【0028】一方、接触ばっ気槽7には、表面に好気性
微生物が付着した接触材11と、浄化槽本体外に別途備
えられた送風機(図示せず)から供給されるエアにより
槽7内にばっ気旋回流を生じさせる散気管12と、逆洗
用の散気管からなる逆洗装置13とが設けられていると
ともに、処理水の流路および清掃孔を兼ねた角筒状の筒
部7aが第2仕切り壁4bに沿って形成されている。そ
して、嫌気ろ床槽第2室6側から接触ばっ気槽7内に流
入した処理水が槽内のばっ気旋回流にのって接触材11
の間を攪拌されながらばっ気循環を繰り返し、その過程
で接触材表面の生物膜の作用を受けてばっ気処理され、
その後、第3仕切り壁4cの下方の連通部4c’を通っ
て沈殿槽8内に流入するようになっている。
On the other hand, in the contact aeration tank 7, the contact material 11 having aerobic microorganisms adhered to the surface thereof and the air supplied from a blower (not shown) separately provided outside the main body of the purification tank are used to enter the inside of the tank 7. An air diffuser 12 for producing an aeration swirl flow and a backwash device 13 composed of an air diffuser for backwashing are provided, and a rectangular tubular portion 7a also serving as a flow path for the treated water and a cleaning hole. Are formed along the second partition wall 4b. Then, the treated water that has flowed into the contact aeration tank 7 from the side of the second chamber 6 of the anaerobic filter bed is placed on the contact material 11 along the aeration swirl flow in the tank.
Repeated aeration circulation while being agitated between the two, and in the process, it is aerated by the action of the biofilm on the contact material surface,
After that, it flows into the settling tank 8 through the communication portion 4c ′ below the third partition wall 4c.

【0029】また、沈殿槽8には、薬剤筒14aや越流
堰14b等を有する消毒槽14が上部に設けられてい
る。そして、接触ばっ気槽7側から流入した処理水が沈
殿槽8内で上澄み水と剥離汚泥とに分離され、その上澄
み水のうち越流堰14を越えて消毒槽14内に流入した
処理水が薬剤により減菌処理された上で流出管3を通じ
て外部に放流される一方、沈殿槽8の傾斜状底部に沈殿
した剥離汚泥は再び接触ばっ気槽7に戻って処理される
ようになっている。
Further, the settling tank 8 is provided with a disinfecting tank 14 having a medicine cylinder 14a, an overflow weir 14b, and the like at its upper part. Then, the treated water that has flowed in from the contact aeration tank 7 side is separated into the supernatant water and the separated sludge in the settling tank 8, and the treated water that has flowed into the disinfection tank 14 beyond the overflow weir 14 in the supernatant water. Is sterilized by chemicals and then discharged to the outside through the outflow pipe 3, while the separated sludge settled on the inclined bottom of the settling tank 8 is returned to the contact aeration tank 7 for further processing. There is.

【0030】さらに、この合併処理浄化槽1において
は、処理水の水質性能をより向上させる手段として、接
触ばっ気槽7内の汚泥を含む処理水を汲み上げるエアリ
フトポンプ15と、その汲み上げられた汚泥を含む処理
水を嫌気ろ床槽第1室5に移送する本発明の特徴部分で
ある汚泥移送装置20とが備えられている。
Further, in the combined treatment septic tank 1, as a means for further improving the water quality performance of the treated water, the air lift pump 15 for pumping the treated water containing sludge in the contact aeration tank 7 and the sludge pumped up. A sludge transfer device 20, which is a characteristic part of the present invention, for transferring the treated water contained therein to the anaerobic filter bed first chamber 5 is provided.

【0031】上記エアリフトポンプ15は、上端部が接
触ばっ気槽7の水位以上の高さ位置に保持され且つ下端
開口部16aが槽底部の近傍に配置された揚水管16
と、この揚水管16の下部に一端が接続された送気管1
7とで構成されており、その送気管17のエア流入部側
には、エア量を調整する例えばニードルバルブでなるエ
ア調整バルブ18が設けられている。そして、上述した
送風機から送気管17を介して揚水管16の下部内に供
給されるエアのリフト作用により揚水管16内の水位を
上げ、これによって接触ばっ気槽7内の汚泥を含む処理
水を揚水管16の下端開口部16aから上端部まで汲み
上げて汚泥移送装置20に供給するようになっている。
The air lift pump 15 has a pumping pipe 16 whose upper end is held at a height higher than the water level of the contact aeration tank 7 and whose lower end opening 16a is arranged near the tank bottom.
And an air pipe 1 having one end connected to the lower portion of the pumping pipe 16.
7, an air adjusting valve 18 for adjusting the amount of air, which is, for example, a needle valve, is provided on the air inflow side of the air supply pipe 17. Then, the water level in the pumping pipe 16 is raised by the lift action of the air supplied from the blower to the lower part of the pumping pipe 16 via the blower pipe 17, whereby the treated water containing sludge in the contact aeration tank 7 is raised. Is pumped up from the lower end opening 16a of the pumping pipe 16 to the upper end and supplied to the sludge transfer device 20.

【0032】一方、本発明の特徴部分である汚泥移送装
置20は、揚水管16の上端部に接続されて管路を2方
向に分岐させるチーズでなる分岐管21と、その分岐さ
れた一方の管端部に基端が接続されて先端が嫌気ろ床槽
第1室5の水位よりも上方に位置する汚泥移送用の第1
配管22と、分岐管21の他方の管端部に接続されて先
端が接触ばっ気槽7の水位よりも上方に位置する返送用
の第2配管23とを有する。
On the other hand, the sludge transfer device 20, which is a characteristic part of the present invention, has a branch pipe 21 made of cheese that is connected to the upper end of the pumping pipe 16 to branch the pipe line in two directions, and one of the branched pipes 21. The first for sludge transfer, in which the base end is connected to the pipe end and the end is located above the water level in the anaerobic filter bed first chamber 5.
It has a pipe 22 and a second pipe 23 for return, which is connected to the other pipe end of the branch pipe 21 and whose tip is located above the water level of the contact aeration tank 7.

【0033】このうち、第1配管22は、図3〜5に拡
大して示すように、基端側から順番に第1直管24、エ
ルボ25、第1異径ソケット26、第2直管27、第2
異径ソケット28および汚泥移送管29を接続した構成
である。この中で比較的大きな管径を有する第2直管2
7の上部側には、外部からその管内が見えるように開口
部27aが形成されており、その開口部27aの下方の
管内に堰27bと流量計27cとが設けられている。
Of these, the first pipe 22 is, as enlarged and shown in FIGS. 3 to 5, the first straight pipe 24, the elbow 25, the first different diameter socket 26, and the second straight pipe in order from the base end side. 27, second
This is a configuration in which the different diameter socket 28 and the sludge transfer pipe 29 are connected. Of these, the second straight pipe 2 having a relatively large pipe diameter
An opening 27a is formed on the upper side of 7 so that the inside of the pipe can be seen from the outside, and a weir 27b and a flow meter 27c are provided in the pipe below the opening 27a.

【0034】上記堰27bは、その上面が略水平に形成
されており、移送中の処理水が第2直管27内を通過す
る際に当該堰27bに当たり且つこれを乗り越えた上で
下流側に流れることにより、その勢いと脈動が抑制され
るようになっている。
The weir 27b has an upper surface formed substantially horizontally, and when the treated water being transferred passes through the inside of the second straight pipe 27, hits the weir 27b and overcomes the weir 27b, and then reaches the downstream side. By flowing, the momentum and pulsation are suppressed.

【0035】また、流量計27cは、上面側がV状に切
り欠かれており、予め求められた実験式により、その切
り欠き部27c’の開き角度と底部からの高さとから、
ここを通過する処理水の流量を概ね推定できるようにし
たもので、その高さ方向には目盛りが付けられている。
そして、堰27bを越えた処理水が流量計27cを通っ
て汚泥移送管29の方向に流れる際に、その処理水の流
量、つまり移送水量の概略値を流量計27cの目盛りを
読むことによって知ることができるようになっている。
Further, the flow meter 27c is notched in a V shape on the upper surface side, and from the opening angle of the notch portion 27c 'and the height from the bottom portion, according to a previously determined empirical formula,
It is designed so that the flow rate of treated water passing therethrough can be roughly estimated, and a scale is attached in the height direction.
Then, when the treated water that has passed over the weir 27b flows in the direction of the sludge transfer pipe 29 through the flow meter 27c, the flow rate of the treated water, that is, the approximate value of the transferred water amount is known by reading the scale of the flow meter 27c. Is able to.

【0036】さらに、この実施例では、特に第1直管2
4と第1異径ソケット26との間にエルボ25が配置さ
れ且つそのエルボ25の折れ曲がり部の外側部分に開口
25aが形成されている。これは、移送される処理水
(汚泥を含む)をエルボ25の折れ曲がり部に当てるこ
とでその流速の変動を緩和するとともに、そのようにし
て処理水がエルボ25に当たって直角方向に流れの向き
を変える時に、その一部を開口25aから外部に流出さ
せることによりエアリフトポンプ15による脈流を抑え
て移送水量を一定に保つためのものである。
Further, in this embodiment, in particular, the first straight pipe 2
An elbow 25 is arranged between the first and second sockets 4 having different diameters, and an opening 25a is formed in an outer portion of the bent portion of the elbow 25. This is because the transferred treated water (including sludge) is applied to the bent portion of the elbow 25 to reduce the fluctuation of the flow velocity thereof, and the treated water thus hits the elbow 25 and changes the direction of the flow in a right angle direction. At this time, a part of the air flow is made to flow out from the opening 25a to suppress the pulsating flow by the air lift pump 15 to keep the amount of transferred water constant.

【0037】一方、第2配管23は、上記分岐管21に
接続された直管30と、この直管30の先端部に回動可
能に接続された戻し用エルボ31とで構成されている。
そして、この戻し用エルボ31を直管30の中心軸に対
して回動させることにより、その軸回りにエルボ31の
先端開口部31aの向き、つまりエルボ31の装着角度
を自由に変えられるようになっている。なお、戻し用エ
ルボ31は、先端開口部31aに蓋(図示せず)が装着
可能とされているとともに、移送水の勢いで脱落しない
ように必要に応じて例えばねじ込み式又はピン若しくは
キー等を差し込むことにより、直管30から抜け落ちな
いようになっている。
On the other hand, the second pipe 23 is composed of a straight pipe 30 connected to the branch pipe 21 and a return elbow 31 rotatably connected to the tip of the straight pipe 30.
By rotating the return elbow 31 with respect to the central axis of the straight pipe 30, the direction of the tip opening 31a of the elbow 31, that is, the mounting angle of the elbow 31, can be freely changed around the axis. Has become. The return elbow 31 has a lid (not shown) that can be attached to the tip opening 31a, and if necessary, for example, a screw-in type or a pin or a key may be attached so as not to fall off due to the force of the transfer water. By being inserted, the straight pipe 30 is prevented from falling off.

【0038】ここで、図例の分岐管21においては、そ
の2方向に分岐した一方の管路側(以下、この方向を分
岐管21の主流の向きという)へ処理水が他方の管路側
よりも流れやすくなるように、分岐側の管部分に対して
流入側の管部分をカーブ状に接続した構成を採用した
が、通常のチーズのようにT状に接続した構成を採用し
てもよいことは勿論である。
Here, in the branch pipe 21 of the illustrated example, the treated water is directed toward one of the two branching sides (hereinafter, this direction is referred to as the main flow direction of the branching pipe 21) rather than the other side. In order to make it easier to flow, the inflow side pipe part is connected to the branch side pipe part in a curved shape, but a structure in which it is connected in a T shape like normal cheese may be adopted. Of course.

【0039】次に、上記実施例の作用を説明する。家庭
から排出された汚水は、まず合併処理浄化槽1の流入管
2を通じて浄化槽本体4内の嫌気ろ床槽第1室5内に導
入される。そして、同室内のろ材9を通過する際にその
表面に生成された嫌気性微生物によって嫌気処理された
後、第1仕切り壁4a側の筒部5aおよび連通口4a’
を通って第2室6内に流入し、さらにこの第2室6でも
同室内のろ材10により再び嫌気処理が行われた上で、
第2仕切り壁4b側の筒部6aおよび連通口4b’を通
って接触ばっ気槽7側に流入する。
Next, the operation of the above embodiment will be described. Sewage discharged from the household is first introduced into the anaerobic filter bed first chamber 5 in the septic tank body 4 through the inflow pipe 2 of the combined treatment septic tank 1. Then, after passing through the filter medium 9 in the same chamber, it is anaerobically treated by the anaerobic microorganisms generated on its surface, and then the tubular portion 5a and the communication port 4a 'on the side of the first partition wall 4a.
Flow into the second chamber 6 through the above, and in the second chamber 6 as well, after the anaerobic treatment is performed again by the filter medium 10 in the same chamber,
It flows into the contact aeration tank 7 side through the cylindrical portion 6a on the second partition wall 4b side and the communication port 4b '.

【0040】次に、この接触ばっ気槽7内に流入した処
理水は、同槽内のばっ気旋回流にのって接触材11の間
を攪拌されながらばっ気循環を繰り返し、その過程で接
触材表面の生物膜の作用を受けてばっ気処理され、その
後、第3仕切り壁4cの下方の連通部4c’を通って沈
殿槽8内に流入する。そして、沈殿槽8内で上澄み水と
剥離汚泥とに分離され、その上澄み水のうち越流堰14
bを越えて薬剤筒14aのある消毒槽14内に流入した
処理水が薬剤により減菌処理された上で流出管3を通じ
て外部に放流される一方、沈殿槽8の傾斜状底部に沈殿
した剥離汚泥は再び接触ばっ気槽7に戻って処理され
る。
Next, the treated water flowing into the contact aeration tank 7 repeats aeration circulation while being agitated between the contact materials 11 along the aeration swirl flow in the same tank, and in the process. Aeration is performed by the action of the biofilm on the surface of the contact material, and then flows into the settling tank 8 through the communication portion 4c ′ below the third partition wall 4c. Then, in the settling tank 8, the supernatant water and the separated sludge are separated, and the overflow weir 14 of the supernatant water is separated.
Treated water that has flowed into the disinfecting tank 14 having the medicine cylinder 14a beyond b is sterilized by the medicine and is then discharged to the outside through the outflow pipe 3, while the separation that has settled on the inclined bottom of the settling tank 8 is performed. The sludge returns to the contact aeration tank 7 again for processing.

【0041】ところで、このような通常の処理過程にお
いては、接触ばっ気槽7における送気管17のエア流入
側に設けられたエア調整バルブ18を閉じておくが、逆
洗作業や循環処理を行う場合には、接触ばっ気槽7内の
接触材11から剥離された汚泥を嫌気ろ床槽第1室5に
移送して同室および第2室6の微生物による脱窒処理に
供する必要があるため、エア調整バルブ18を開いて揚
水管16にエアを供給し、そのエアリフト作用によって
接触ばっ気槽7内の剥離汚泥を含む処理水を揚水管16
の上端部に接続された汚泥移送装置20に送る。
By the way, in such a normal process, the air adjusting valve 18 provided on the air inflow side of the air supply pipe 17 in the contact aeration tank 7 is closed, but the backwashing work and the circulation process are performed. In this case, it is necessary to transfer the sludge separated from the contact material 11 in the contact aeration tank 7 to the first chamber 5 of the anaerobic filter bed tank for denitrification treatment by the microorganisms in the same chamber and the second chamber 6. , The air adjusting valve 18 is opened to supply air to the pumping pipe 16, and the air lift action causes the treated water containing the separated sludge in the contact aeration tank 7 to be pumped up.
To the sludge transfer device 20 connected to the upper end of the.

【0042】その場合、逆洗の時には、第2配管23に
おけるエルボ31を図3の鎖線で示すように上向きに
し、その先端開口部31aに蓋(図示せず)をしてお
く。そして、接触ばっ気槽7における散気管12へのエ
アの供給を停止して、揚水管16には送気管17を介し
て多量のエアを供給する。このようにすると、揚水管1
6を通じて汲み上げられた汚泥を含む処理水は、接触ば
っ気槽7に戻らず、その全て(例えば、50〜100リ
ットル/分)が第2配管22を通って嫌気ろ床槽第1室
5に移送されることとなる。
In this case, at the time of backwashing, the elbow 31 in the second pipe 23 is directed upward as shown by the chain line in FIG. 3, and the tip opening 31a is covered with a lid (not shown). Then, the supply of air to the diffuser pipe 12 in the contact aeration tank 7 is stopped, and a large amount of air is supplied to the pumping pipe 16 via the air supply pipe 17. In this way, pumping pipe 1
The treated water containing sludge pumped through 6 does not return to the contact aeration tank 7, and all (for example, 50 to 100 liters / minute) passes through the second pipe 22 to the anaerobic filter tank first chamber 5. Will be transferred.

【0043】一方、循環時には、図3の実線で示すよう
に、上記エルボ31を下向きにし、その先端開口部31
aには蓋をしないでおく。また、揚水量が少量となるよ
うにエア調整バルブ18を絞るとともに、接触ばっ気槽
7における散気管12にはエアを供給して、ばっ気旋回
流を生じさせておく。このようにすると、揚水管16を
通じて汲み上げられた汚泥を含む処理水は、分岐管21
によって2方向に分岐され、一部がエルボ31を介して
接触ばっ気槽7に戻されるとともに、その残りが第2配
管22を通じて嫌気ろ床槽第1室5に移送されることと
なる。
On the other hand, at the time of circulation, as shown by the solid line in FIG.
Do not cover a. Further, the air adjusting valve 18 is throttled so that the amount of pumped water becomes small, and air is supplied to the diffuser pipe 12 in the contact aeration tank 7 to generate an aeration swirl flow. By doing so, the treated water containing the sludge pumped up through the pumping pipe 16 will not flow into the branch pipe 21.
Is branched in two directions, and a part of it is returned to the contact aeration tank 7 via the elbow 31, and the rest is transferred to the anaerobic filter tank first chamber 5 through the second pipe 22.

【0044】この時、短絡等の問題が生じないように、
処理水は、嫌気ろ床槽5へ一定の割合で供給されなけれ
ばならず、そのためには第2配管22内を流れる処理水
の流量を知る必要があるが、揚水管16を通じて分岐管
21内まで汲み上げられた処理水にはエアリフトポンプ
15による脈動が伴うため、そのままでは流量を推定す
るのが難しい。
At this time, in order not to cause a problem such as a short circuit,
The treated water must be supplied to the anaerobic filter bed tank 5 at a constant rate, and in order to do so, it is necessary to know the flow rate of the treated water flowing through the second pipe 22. It is difficult to estimate the flow rate as it is because the treated water pumped up to is accompanied by pulsation by the air lift pump 15.

【0045】しかし、この実施例の汚泥移送装置20に
おいては、第2配管22にエルボ25が設けられて、そ
の折れ曲がり部の外側部分に開口25aが形成されてい
るとともに、その更に下流側には、比較的大径の第2直
管27の管上部側に開口部27aが形成され、この開口
部27aの下方の管内に堰27bとV状の切り欠き27
c’を有する流量計27cとが設けられている。
However, in the sludge transfer device 20 of this embodiment, the elbow 25 is provided in the second pipe 22, the opening 25a is formed in the outer portion of the bent portion, and further downstream thereof. An opening 27a is formed on the upper side of the second straight pipe 27 having a relatively large diameter, and a weir 27b and a V-shaped notch 27 are formed in the pipe below the opening 27a.
and a flow meter 27c having c '.

【0046】従って、分岐管21側から第2配管22内
に送られてきた処理水(移送水)は、まずエルボ25の
折り曲がり部に当たって流速の変動が緩和されると同時
に、その一部を折れ曲がり部の開口25aから外部に流
出させつつ、直角方向に流れの向きを変える。その結
果、処理水は脈動が或る程度抑えられた上で、下流側の
第1異径ソケット26を介して流路を拡大されつつ第2
直管27に到る。そして、この第2直管27において
も、開口部27aの下方の堰27bに当たって更に脈動
と勢いが抑制されることにより、その堰27bを越えた
処理水は、比較的脈動の少ない定常流に近いものとな
り、その状態で下流側の流量計27cを通過する。
Therefore, the treated water (transferred water) sent from the side of the branch pipe 21 into the second pipe 22 first hits the bent portion of the elbow 25 to reduce the fluctuation of the flow velocity, and at the same time, part of the treated water is transferred. The flow direction is changed in the perpendicular direction while flowing out from the opening 25a of the bent portion to the outside. As a result, the pulsation of the treated water is suppressed to a certain extent, and the flow path is expanded through the first socket of different diameter 26 on the downstream side to the second side.
The straight pipe 27 is reached. Also in the second straight pipe 27, the pulsation and the momentum are further suppressed by hitting the weir 27b below the opening 27a, so that the treated water that has passed over the weir 27b is close to a steady flow with relatively little pulsation. In this state, it passes through the flowmeter 27c on the downstream side.

【0047】その際、流量計27cは開口部27aの下
方に配置されており、そのV状の切り欠き27c’を通
過する処理水の水位がわかるように高さ方向に目盛りが
付けられているから、その目盛りを外部から目視によっ
て読み取ることによって、その時点の処理水の流量、つ
まり移送水量の概略値を簡単に知ることができる。従っ
て、こうして読み取った移送水量に基づいて、例えば上
記エア調整バルブ18により揚水量を加減するなどする
ことにより、嫌気ろ床槽第1室5と接触ばっ気槽7との
間で一定の割合(例えば、1〜5リットル/分)の処理
水を循環させることができる。
At this time, the flow meter 27c is arranged below the opening 27a and is graduated in the height direction so that the water level of the treated water passing through the V-shaped notch 27c 'can be seen. From this, by visually reading the scale from the outside, it is possible to easily know the flow rate of the treated water at that time, that is, the approximate value of the transferred water amount. Therefore, based on the transfer water amount read in this way, for example, by adjusting the pumping amount by the air adjusting valve 18, the anaerobic filter tank first chamber 5 and the contact aeration tank 7 have a constant ratio ( For example, 1 to 5 l / min) of treated water can be circulated.

【0048】なお、この実施例に係る合併処理浄化槽1
は、嫌気ろ床槽として第1室5及び第2室6を有する嫌
気ろ床接触ばっ気方式のものであるが、本発明の適用対
象は、このようなタイプの合併処理浄化槽に限られるも
のではない。例えば、嫌気ろ床槽を有しないもの或いは
1室しかないもの、嫌気ろ床槽に代えて沈殿分離槽を設
けた分離接触ばっ気方式のもの、さらには嫌気ろ床槽に
隣接させてその上流側に沈殿分離槽を併設したもの等の
各種タイプの合併処理浄化槽に適用することが可能であ
る。
The combined treatment septic tank 1 according to this embodiment
Is an anaerobic filter contact aeration system having a first chamber 5 and a second chamber 6 as an anaerobic filter bed, but the application of the present invention is limited to such type of combined treatment septic tank. is not. For example, those that do not have an anaerobic filter bed or have only one room, those that use a separation contact aeration system that has a precipitation separation tank in place of the anaerobic filter bed, and that are adjacent to the anaerobic bed tank and that upstream. It can be applied to various types of combined treatment septic tanks such as a side with a sedimentation separation tank.

【0049】[0049]

【発明の効果】以上のように、本発明によれば、接触ば
っ気槽内の汚泥を含む処理水の一部を揚水して嫌気ろ床
槽等に移送するようにした合併処理浄化槽の汚泥移送装
置において、上記汚泥を含む処理水の脈動、つまり移送
水の脈動を効果的に防止することができるから、その移
送水の流量計測とそれに基づく流量調整とを容易に行う
ことができる。
As described above, according to the present invention, the sludge of the combined treatment septic tank in which a part of the treated water containing the sludge in the contact aeration tank is pumped up and transferred to the anaerobic filter tank or the like. In the transfer device, the pulsation of the treated water containing the sludge, that is, the pulsation of the transfer water can be effectively prevented, so that the flow rate measurement of the transfer water and the flow rate adjustment based thereon can be easily performed.

【0050】しかも、上記脈動の防止と流量計測とを行
う手段としては、分岐管から嫌気ろ床槽等に到る配管の
途中に開口部を形成し且つその下方の管内に堰とV状の
切り欠きを有する簡易な流量計とを設けただけであるか
ら、比較的簡素な構成で、保守点検や管理も容易に行え
ることとなる。
Moreover, as a means for preventing the pulsation and measuring the flow rate, an opening is formed in the middle of the pipe from the branch pipe to the anaerobic filter tank, and a weir and V-shape are formed in the pipe below the pipe. Since only a simple flow meter having a notch is provided, maintenance and inspection can be easily performed with a relatively simple structure.

【0051】さらに、従来のように箱状の流量計を別途
設ける必要がないので、バルブ等が比較的多く集まって
いる揚水管上部周辺に大きな設置スペースを取ることも
ない。
Further, since it is not necessary to separately provide a box-shaped flow meter as in the conventional case, a large installation space is not required around the upper part of the pumping pipe where a relatively large number of valves and the like are gathered.

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

【図1】本発明の一実施例に係る合併処理浄化槽の全体
構成を示す概略平面図
FIG. 1 is a schematic plan view showing the overall configuration of a combined treatment septic tank according to an embodiment of the present invention.

【図2】同浄化槽の概略縦断面図FIG. 2 is a schematic vertical sectional view of the septic tank.

【図3】同浄化槽に備えられた汚泥移送装置を示す図2
の右側面から見た側面図
FIG. 3 is a view showing a sludge transfer device provided in the septic tank.
Side view from the right side

【図4】同汚泥移送装置の一部を示す部分平面図FIG. 4 is a partial plan view showing a part of the sludge transfer device.

【図5】同汚泥移送装置の一部を切り欠いて示す部分正
面図
FIG. 5 is a partial front view showing a cutaway part of the sludge transfer device.

【図6】図5のA−A線で切断した断面図6 is a cross-sectional view taken along the line AA of FIG.

【図7】図5のB−B線で切断した断面図FIG. 7 is a sectional view taken along line BB in FIG.

【符号の説明】[Explanation of symbols]

1・・・合併処理浄化槽本体 5、6・・・嫌気ろ床槽(5・・・第1室、6・・・第
2室) 16・・・揚水管 17・・・送気管 18・・・エア量調整バルブ 20・・・汚泥移送装置 21・・・分岐管 22・・・配管(第1配管) 27a・・・開口部 27b・・・堰 27c・・・流量計 27c’・・・V状の切り欠き部
1 ... Merged treatment septic tank body 5, 6 ... Anaerobic filter bed tank (5 ... 1st chamber, 6 ... 2nd chamber) 16 ... Pumping pipe 17 ... Air supply pipe 18 ... -Air amount adjusting valve 20 ... Sludge transfer device 21 ... Branch pipe 22 ... Piping (first piping) 27a ... Opening portion 27b ... Weir 27c ... Flowmeter 27c '... V-shaped notch

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 流入する汚水を嫌気処理する嫌気ろ床槽
又は沈殿分離処理する沈殿分離槽と、その嫌気又は沈殿
分離処理された処理水を好気処理する接触ばっ気槽と、
この接触ばっ気槽内の処理水を揚水する揚水管と、この
揚水管の下部に一端が接続されて送風機からのエアを揚
水管内に供給する送気管と、この送気管を介して揚水管
内に供給されるエアの量を調整するエア量調整バルブと
を有し、上記揚水管により接触ばっ気槽内の汚泥を含む
処理水の一部を揚水して嫌気ろ床槽又は沈殿分離槽に移
送するようにした合併処理浄化槽の汚泥移送装置であっ
て、上記揚水管の上端部が分岐管を介して2方向に分岐
されており、その分岐された一方の端部が嫌気ろ床槽又
は沈殿分離処理槽の上部に、他方の端部が接触ばっ気槽
内の上部にそれぞれ位置するように配管されているとと
もに、上記分岐管から嫌気ろ床槽又は沈殿分離層の上部
に到る配管の途中の管上部側に開口部が形成されてお
り、その開口部の下方の管内に、移送される処理水の脈
動を抑制する堰と、この堰を越えて嫌気ろ床槽又は沈殿
分離層の方に流れる処理水の流量を計測するV状の切り
欠き部を有する流量計とが設けられていることを特徴と
する合併処理浄化槽の汚泥移送装置。
1. An anaerobic filter bed tank for anaerobically treating inflowing wastewater or a sedimentation separation tank for sedimentation separation treatment, and a contact aeration tank for aerobically treating the treated water that has undergone anaerobic or sedimentation separation treatment.
A pumping pipe for pumping the treated water in the contact aeration tank, an air supply pipe with one end connected to the lower part of the pumping pipe to supply air from the blower into the pumping pipe, and a pumping pipe through the air supply pipe into the pumping pipe. It has an air amount adjustment valve that adjusts the amount of air supplied, and a portion of the treated water containing sludge in the contact aeration tank is pumped by the above-mentioned pumping pipe and transferred to the anaerobic filter tank or sedimentation separation tank. In the sludge transfer device of the combined treatment septic tank, the upper end of the pumping pipe is branched into two directions via a branch pipe, and one end of the branch is an anaerobic filter tank or a sedimentation tank. In the upper part of the separation treatment tank, the other end is arranged so that it is located in the upper part of the contact aeration tank, and the pipe from the branch pipe to the upper part of the anaerobic filter bed tank or the sedimentation separation layer. An opening is formed on the upper side of the pipe in the middle, and below the opening. With a weir that suppresses the pulsation of the transferred treated water and a V-shaped notch that measures the flow rate of the treated water that flows over the weir toward the anaerobic filter bed or sedimentation separation layer A sludge transfer device for a combined treatment septic tank, which is provided with a meter.
JP11052193A 1993-05-12 1993-05-12 Sludge transfer device for combined treating septic tank Pending JPH06320181A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11052193A JPH06320181A (en) 1993-05-12 1993-05-12 Sludge transfer device for combined treating septic tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11052193A JPH06320181A (en) 1993-05-12 1993-05-12 Sludge transfer device for combined treating septic tank

Publications (1)

Publication Number Publication Date
JPH06320181A true JPH06320181A (en) 1994-11-22

Family

ID=14537911

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11052193A Pending JPH06320181A (en) 1993-05-12 1993-05-12 Sludge transfer device for combined treating septic tank

Country Status (1)

Country Link
JP (1) JPH06320181A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005185892A (en) * 2003-12-24 2005-07-14 Fuji Clean Kogyo Kk Sewage treatment device
JP2012050955A (en) * 2010-09-03 2012-03-15 Fuji Clean Co Ltd Transfer pipe and device for treating waste water

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005185892A (en) * 2003-12-24 2005-07-14 Fuji Clean Kogyo Kk Sewage treatment device
JP4554194B2 (en) * 2003-12-24 2010-09-29 フジクリーン工業株式会社 Sewage treatment equipment
JP2012050955A (en) * 2010-09-03 2012-03-15 Fuji Clean Co Ltd Transfer pipe and device for treating waste water

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