JP2587460Y2 - Septic tank - Google Patents

Septic tank

Info

Publication number
JP2587460Y2
JP2587460Y2 JP1991043893U JP4389391U JP2587460Y2 JP 2587460 Y2 JP2587460 Y2 JP 2587460Y2 JP 1991043893 U JP1991043893 U JP 1991043893U JP 4389391 U JP4389391 U JP 4389391U JP 2587460 Y2 JP2587460 Y2 JP 2587460Y2
Authority
JP
Japan
Prior art keywords
tank
liquid level
water
treated
air
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
JP1991043893U
Other languages
Japanese (ja)
Other versions
JPH04137799U (en
Inventor
八郎 佐藤
丈衛 佐藤
良人 北井
大 原田
和之 本田
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 JP1991043893U priority Critical patent/JP2587460Y2/en
Publication of JPH04137799U publication Critical patent/JPH04137799U/en
Application granted granted Critical
Publication of JP2587460Y2 publication Critical patent/JP2587460Y2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Jet Pumps And Other Pumps (AREA)
  • Treatment Of Biological Wastes In General (AREA)

Description

【考案の詳細な説明】[Detailed description of the invention]

【0001】[0001]

【産業上の利用分野】本考案は、複数の処理槽を流路方
向に直列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 in which a plurality of processing tanks are provided in series in a flow direction.

【0002】[0002]

【従来の技術】従来、この種の浄化槽にあっては、隣接
する前記処理槽において上流側の処理槽から下流側の処
理槽へ被処理水を送るのに、被処理水をオーバーフロー
させる堰を設け、自然移流させる構成のものが用いられ
ていた。
2. Description of the Related Art Conventionally, in this type of purification tank, a weir for overflowing the water to be treated is provided in the adjacent treatment tank for sending the water to be treated from an upstream treatment tank to a downstream treatment tank. In this case, a natural advection was used.

【0003】[0003]

【考案が解決しようとする課題】ところが、このような
浄化槽では、上流側の処理槽に流入する処理水の流量が
大きくなれば、水位が上がり、水位が上がるとオーバー
フロー量も大きくなる。従って、例えば、ピークの流入
時に処理能力以上の処理水が流入すると、これが充分に
処理されないまま移流して、最終的に放流される排水中
の浮遊懸濁物やBODが規制値を越える虞があった。そ
こで、本考案の目的は、上流側の処理槽への被処理水の
流量に多少の変動があっても、略一定の平均的な流量で
被処理水を下流側の処理槽に送り、安定した生物処理を
行うことのできる浄化槽を提供することにある。
However, in such a purification tank, if the flow rate of the treated water flowing into the upstream treatment tank increases, the water level rises, and if the water level rises, the overflow amount also increases. Therefore, for example, when treated water having a treatment capacity or more flows in at the time of peak inflow, the treated water is advected without being sufficiently treated, and there is a possibility that suspended solids and BOD in the wastewater finally discharged exceed regulatory values. there were. Therefore, the purpose of the present invention is to send the water to be treated to the downstream treatment tank at a substantially constant average flow rate even if there is some fluctuation in the flow rate of the water to be treated to the treatment tank on the upstream side. Another object of the present invention is to provide a septic tank capable of performing a biological treatment.

【0004】[0004]

【課題を解決するための手段】この目的を達成するた
め、本考案による浄化槽の特徴構成は、複数の処理槽
(T1,T2)を流路方向に直列に設けた浄化槽であっ
て、隣接する前記処理槽(T2)の上流側の前記処理槽
(T1)内にエアーリフトポンプ装置(J)を設けると
共に、そのエアーリフトポンプ装置(J)を、一端側を
上方に開口するとともに、揚水した被処理水を下流側の
前記処理槽(T2)に排出する排出路(H)に接続自在
に形成し、他端側を上流側の前記処理槽(T1)内に開
口させてあるU字管を設けるとともに、その排出路の下
流側に前記エアーリフトポンプ装置(J)の被処理水を
下流側に排出する落し口(1c)を設け、かつ、前記一
端側にエアーリフト用エアー供給管(2)を挿入して、
その開口部を前記U字管とは独立して上下移動自在に形
成してエアー供給部(K)を設けて構成し、前記上流側
の処理槽(T1)の液面を検出する液面検出手段(L)
を設け、前記液面検出手段(L)の検出結果に基づき、
前記液面の上下に追従して前記エアー供給部(K)を、
前記落し口(1c)に対して上下移動せて、上流側の処
理槽の液面の上下変動量の割合に対する移送流量の変動
を小さくする連動手段を設けてある事にあることにあ
る。
In order to achieve the object, a characteristic structure of a septic tank according to the present invention includes a plurality of treatment tanks.
(T1, T2) is a septic tank provided in series in the flow path direction.
And the processing tank on the upstream side of the adjacent processing tank (T2)
When an air lift pump device (J) is installed in (T1)
In both cases, the air lift pump device (J)
Opened upwards and pumped water to be treated
Connectable to the discharge path (H) for discharging to the processing tank (T2)
And the other end is opened in the processing tank (T1) on the upstream side.
A U-shaped pipe is provided at the bottom of the discharge channel.
Water to be treated by the air lift pump device (J)
An outlet (1c) for discharging downstream is provided, and
Insert the air supply pipe for air lift (2) into the end side,
The opening is vertically movable independently of the U-shaped tube.
And an air supply unit (K) is provided.
Level detecting means (L) for detecting the level of the processing tank (T1)
And based on the detection result of the liquid level detection means (L),
The air supply unit (K) follows up and down the liquid level,
By moving up and down with respect to the outlet (1c),
Fluctuation of transfer flow rate to ratio of vertical fluctuation of liquid level
In that interlocking means for reducing
You.

【0005】[0005]

【作用】前記エアーリフトポンプ装置を設け、これによ
って揚水した被処理水を下流側の処理槽に排出する排出
路を設けてあると、従来のような自然移流によらず、エ
アーリフトポンプ装置によって揚水した被処理水だけを
前記排出路から下流側の前記処理槽に排出することがで
きるので、移送流量の調整が行いやすい。前記エアーリ
フトポンプ装置へのエアー供給部を上下移動自在に設
け、前記上流側の処理槽の液面を検出する液面検出手段
を設け、前記液面検出手段の検出結果に基づき、前記液
面の上下に追従して前記エアー供給部を上下に連動させ
る連動手段を設けてあるので、前記液面が上下に変動し
ても前記エアー供給部の前記液面からの深さを一定に保
つことができる。
If the air lift pump device is provided and a discharge path for discharging the water to be treated pumped to the downstream processing tank is provided, the air lift pump device can be used instead of the conventional natural advection. Since only the pumped water to be treated can be discharged from the discharge path to the treatment tank on the downstream side, the transfer flow rate can be easily adjusted. An air supply unit for the air lift pump device is provided so as to be vertically movable, and a liquid level detecting means for detecting a liquid level of the upstream processing tank is provided. The liquid level is detected based on a detection result of the liquid level detecting means. Since the interlocking means for interlocking the air supply unit up and down by following up and down is provided, the depth of the air supply unit from the liquid surface is kept constant even if the liquid surface fluctuates up and down. Can be.

【0006】[0006]

【考案の効果】上流側の処理槽から下流側の処理槽への
処理液の移送はエアーリフトポンプ装置で行うため、従
来のオーバーフローによる自然移流に比べると、簡単な
構成をとりながらも、液面の上下に伴う移送流量の変動
を小さくできる。又、電動モータ付の定量ポンプで処理
液を移送することも考えられるが、この場合は、清澄な
処理液でなければ目詰まり等のトラブルが生じ易いのに
比し、エアーリフトポンプ装置による場合は、可動部品
が無く、過負荷や空運転に起因する故障もないので保守
管理が容易である。又、前記液面が上下に変動しても前
記エアー供給部の前記液面からの深さを一定に保つこと
ができる構成にしてあるから、例えば、前記液面が上昇
するとそれだけ前記エアー供給部の深さが増す通常の固
定エアーリフトによる場合よりも、前記液面の上下に伴
う移送流量の変動を更に小さくすることができる。詳述
すれば、前記従来のエアリフトポンプ装置によれば、液
面の上昇により、その液面変動分だけ、つまり、前記液
面から落し口までの距離が減少する分だけ、揚底を上昇
させるだけでなく、液面下のエアリフト長さが増加する
分だけエア供給長さが増加して、揚底を上昇させる効果
を発揮してしまうという相乗効果により被処理水の移送
量を増大させることになるのであるが、これに対して、
本発明の構成によれば、前記液面から落し口までの距離
が減少する分だけの揚底上昇に相当する移送量増大だけ
で済み、例えば、上流側に大量の被処理水が流入したと
きに、単に被処理水を定流量で移送していたのでは、上
流側の槽に被処理水が長期にわたって滞留するようなこ
とがあり得るのに対して、上流側から下流側への被処理
水移送量を確保しながらも、前記従来の構成に比べて、
被処理水移送量は、変動が少なくなり、より一定に保て
るようになったのである。また、処理液を揚水する上端
面は固定されることになるから、前記排出部との相対位
置が固定され、特に大きなスペースを要することなく、
エアーリフトポンプ装置を設けることができる。さら
に、上下移動するのは、前記エアー供給管のみで、エア
ーリフトポンプ装置全体が上下移動するものでもないか
ら、液面検出手段による液面検出にエアー供給部の上下
移動を追従させるにも、小さな力で対応できるから、例
えば、フ ロートを設けるだけの簡単な構成ですみ、やは
り、小さなスペースでエアーリフトポンプ装置全体を構
成することができる。尚、エアー供給部の上下移動とエ
アーを供給するブロワ等との接続についても、単に可撓
性ホースを接続するだけの簡便なものを採用できる。
って、生物処理の負荷変動を小さく抑えることが出来る
と共に、前記エアー供給部の液面からの深さが一定であ
ることによるだけでも、前記エアーリフトポンプ用エア
ー圧の変動が小さくなるので、例えば、接触ばっ気槽に
おける散気用エアーと同じエアー供給源から前記エアー
リフトポンプ用エアーを供給しても、散気用エアー圧を
略一定に保つことができる。このため、槽内の循環流や
溶存酸素量も一定の状態に保ち易い。つまり、上記の構
成によって、維持管理が容易でありながら、上流側の処
理槽への被処理水の流量に多少の変動があっても、略一
定の平均的な流量で被処理水を下流側の処理槽に送り、
安定した生物処理を行うことのできる浄化槽を、極めて
簡単な構成で、かつ、浄化槽内のスペースをあまり圧迫
することなく提供することができた。しかも、上流側の
水位変動に対して、ある程度被処理水移送量の変化を残
して、上流側の水位変動の影響を早期に解消でき、か
つ、下流側の水位変動の影響も抑制できたのである。
[Effect of the Invention] Since the transfer of the processing liquid from the upstream processing tank to the downstream processing tank is performed by an air lift pump device, the liquid processing liquid has a simpler structure than the conventional natural advection due to overflow, but has a simple structure. Fluctuations in the transfer flow rate due to the vertical movement of the surface can be reduced. It is also conceivable that the processing liquid is transferred by a metering pump equipped with an electric motor.In this case, however, troubles such as clogging are likely to occur unless the processing liquid is clear. Since there are no moving parts and no troubles caused by overload or idling, maintenance is easy. Also, since the depth of the air supply unit from the liquid level can be kept constant even if the liquid level fluctuates up and down, for example, when the liquid level rises, the air supply unit The fluctuation of the transfer flow rate due to the rise and fall of the liquid level can be further reduced as compared with the case of a normal fixed air lift in which the depth of the liquid increases. More specifically, according to the conventional air lift pump device, when the liquid level rises, the lift is raised by an amount corresponding to the fluctuation of the liquid level, that is, by an amount corresponding to a decrease in the distance from the liquid level to the outlet. Not only that, the amount of air to be treated is increased by the synergistic effect that the air supply length is increased by the amount of the air lift length below the liquid level and the effect of raising the lifting bottom is exhibited. , But on the other hand,
According to the configuration of the present invention, it is only necessary to increase the transfer amount corresponding to the lifting of the bottom by the amount by which the distance from the liquid surface to the drop is reduced, for example, when a large amount of water to be treated flows into the upstream side However, simply transferring the water to be treated at a constant flow rate may cause the water to remain in the upstream tank for a long period of time, whereas the water to be treated from the upstream to the downstream may be While securing the water transfer amount, compared to the conventional configuration,
The transfer rate of the water to be treated has become less variable and can be kept more constant. The upper end for pumping the processing liquid
Since the surface is fixed, it is positioned relative to the discharge section.
Position is fixed, without requiring a particularly large space,
An air lift pump device can be provided. Further
Only the air supply pipe moves up and down.
-Is the entire lift pump device moving up and down?
The upper and lower air supply units to detect the liquid level by the liquid level detection means.
For example, you can follow the movement with a small force.
In example, the corner with a simple configuration of only providing a float, ya
The entire air lift pump device in a small space.
Can be achieved. Note that the vertical movement of the air supply
Connection with a blower that supplies air
It is possible to adopt a simple one that simply connects a sex hose. Therefore, the variation in the load of the biological treatment can be reduced, and the variation in the air pressure for the air lift pump is reduced only by the fact that the depth of the air supply unit from the liquid surface is constant. Even if the air for the air lift pump is supplied from the same air supply source as the air for air diffusion in the contact aeration tank, the air pressure for air diffusion can be kept substantially constant. For this reason, it is easy to keep the circulating flow and the dissolved oxygen amount in the tank constant. In other words, with the above-described configuration, while the maintenance and management is easy, even if there is some fluctuation in the flow rate of the water to be treated to the treatment tank on the upstream side, To the processing tank,
Septic tanks that can perform stable biological treatment are extremely
With a simple configuration, and too much space in the septic tank
Could be provided without having to do so. Moreover, with respect to the upstream water level fluctuation, the effect of the upstream water level fluctuation was able to be eliminated at an early stage, leaving the change in the amount of transferred water to some extent, and the effect of the downstream water level fluctuation was also suppressed. is there.

【0007】[0007]

【実施例】図1に側断面図を示すように、上流側から、
嫌気濾床槽第1室N1、嫌気濾床槽第2室N2、接触ば
っ気槽第1室E1、接触ばっ気槽第2室E2、沈殿槽
P、消毒槽Sの処理槽を設けて浄化槽を構成してある。
嫌気濾床槽第1室、第2室N1,N2は、被処理水中の
有機物を嫌気分解する嫌気性微生物を育成して、その生
物膜を定着させるための濾床F1、F2を設けてあり、
ここでは、ばっ気を行わない。接触ばっ気槽第1室、第
2室E1,E2は、被処理水中の有機物等を酸化分解す
る好気性微生物を育成定着させるための接触材C1,C
2を設け、槽内に被処理水の循環流を生ぜしめて、有機
物を含有する被処理水を、前記接触材C1,C2に育成
定着させた好気性微生物とよく接触させながら、この好
気性微生物に酸素を与えるためのばっ気用エアーを供給
する散気管D1,D2を設けてある。接触ばっ気槽第2
室E2で処理された被処理水は底部から沈殿槽Pに移
り、沈殿槽Pの上澄み液は消毒槽Sを経て放流管11か
ら放流されるようにしてある。流入管10から流入する
被処理水の流量に伴って、嫌気濾床槽第1室N1からの
被処理水が濾床F1の底部から上昇して嫌気濾床槽第2
室N2側にオーバーフローし、濾床F2の底部に自然移
流するように、嫌気濾床槽第1室N1と嫌気濾床槽第2
室N2との間の隔壁5には、1対の移流管L1,L2を
浄化槽の流路方向中心線に対して左右対称に設けてあ
る。嫌気濾床槽第2室N2と接触ばっ気槽第1室E1の
間の隔壁13には上部中央に1箇所自然移流によるオー
バーフロー部V3を設けてある。図2及び図3に要部平
面図及び側断面図を示すように上流側・下流側の処理槽
として接触ばっ気槽第一室(E1)第二室(E2)を適
用した場合には、接触ばっ気槽第1室E1(T1)と接
触ばっ気槽第2室E2(T2)の間の隔壁14には自然
移流によるオーバーフロー部を設けず、代わりに接触ば
っ気槽第1室E1(T1)内にエアーリフトポンプ装置
Jを設けると共に、前記エアーリフトポンプ装置Jによ
って揚水した被処理水を一旦貯留する定ヘッド貯留槽の
役目とエアー抜き口の役目を兼ねる蓋の無い箱状の定ヘ
ッドボックス1を両接触ばっ気槽第1室、第2室E1
(T1),E2(T2)の液面よりも高い位置に設け、
前記定ヘッドボックス1には、中仕切り1dにVノッチ
を形成した下流側へのオーバーフロー部1aと落し口1
cを経由して被処理水を接触ばっ気槽第2室E2(T
2)に排出する排出路Hを設けてある。前記エアーリフ
トポンプ装置Jは中空のパイプをJ字状に形成し、エア
ーリフトポンプ装置Jへのエアー供給部Kたる開口部を
下端に形成したエアーリフト用エアー供給管2の上端を
ブロワーからの給気管3に可撓性ホース4を介して連通
し、前記エアーリフト用エアー供給管2を上下移動自在
にエアーリフトポンプ装置Jの上部より挿入すると共
に、接触ばっ気槽第1室E1(T1)の液面を検出する
液面検出手段たるフロートLを設け、前記エアー供給管
2にフロートLを剛性連結し、フロートLの上下変動に
基づき、前記液面の上下に追従してエアー供給部Kを上
下に連動させる連動手段を構成してある。前記定ヘッド
ボックス1には、接触ばっ気槽第1室E1(T1)側の
側壁1eの上部を水平に切り欠いて形成したオーバーフ
ロー部1bを前記下流側へのオーバーフロー部1aより
もやや高い位置に設け、エアーリフトポンプ装置Jによ
って揚水した被処理水の流量が例え大きくなりすぎて
も、オーバーフロー部1bからオーバーフローさせるこ
とによって下流側への流量を略一定に保つことができる
ようにすると共に、オーバーフロー部1bからオーバー
フローした被処理水を嫌気濾床槽第1室N1に返送する
樋状の返送路Bを設けてある。尚、例えば据え付け時等
に浄化槽の姿勢に多少の狂いが生じても、前記返送路B
の勾配を適宜簡単に修正できるように前記エアーリフト
ポンプ装置Jの上部は可撓性のパイプにしてある。又、
例えば浄化槽への被処理水の流入が比較的長い間止まる
ようなことがあっても、接触ばっ気槽第1室E1(T
1)の液面が下がりすぎることがないよう前記エアーリ
フトポンプ装置Jの吸込口J1は、液面の管理下限の高
さに設けてある。以上の構成によって、例えば浄化槽へ
の被処理水流入量に多少の変動があっても、或は又、エ
アーリフトポンプ装置Jの揚水量をやや大きめに設定し
ても略一定の平均的な流量で被処理水を下流側の処理槽
に送ることができるので、維持管理が容易でありなが
ら、安定した生物処理を行うことのできる浄化槽を提供
することができた。尚、上記エアリフトポンプ装置は嫌
気濾床槽第2室N2等に設置しても良い。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS As shown in FIG.
Anaerobic filter bed tank first chamber N1, anaerobic filter bed tank second chamber N2, contact aeration tank first chamber E1, contact aeration tank second chamber E2, settling tank P, disinfection tank S, and treatment tanks are provided. Is configured.
The first and second chambers anaerobic filter tanks N1 and N2 are provided with filter beds F1 and F2 for growing anaerobic microorganisms that anaerobically decompose organic substances in the water to be treated and fixing the biofilm. ,
In this case, we do not do anything. The first and second chambers E1 and E2 of the contact aeration tank are provided with contact materials C1 and C for growing and fixing aerobic microorganisms that oxidatively decompose organic substances and the like in the water to be treated.
2 is provided, a circulating flow of the water to be treated is generated in the tank, and the water to be treated containing the organic matter is brought into good contact with the aerobic microorganisms grown and fixed on the contact materials C1 and C2. Air diffusion tubes D1 and D2 for supplying aeration air for supplying oxygen to the air are provided. Contact aeration tank second
The water to be treated in the chamber E2 is transferred from the bottom to the sedimentation tank P, and the supernatant of the sedimentation tank P is discharged from the discharge pipe 11 through the disinfection tank S. With the flow rate of the water to be treated flowing from the inflow pipe 10, the water to be treated from the first anaerobic filter tank N1 rises from the bottom of the filter bed F1 and rises from the bottom of the anaerobic filter tank second.
The anaerobic filter tank first chamber N1 and the anaerobic filter tank second overflow so as to overflow to the chamber N2 side and naturally flow to the bottom of the filter bed F2.
A pair of advection tubes L1 and L2 are provided symmetrically with respect to the center line in the flow direction of the septic tank in the partition wall 5 between the chamber N2. The bulkhead 13 between the anaerobic filter tank second chamber N2 and the contact aeration tank first chamber E1 is provided with an overflow portion V3 by natural advection at one place in the upper center. As shown in the plan view and the side sectional view of the main part in FIGS. 2 and 3, the upstream and downstream processing tanks
The first room (E1) and the second room (E2)
When used, the partition 14 between the contact aeration tank first chamber E1 (T1) and the contact aeration tank second chamber E2 (T2) is not provided with an overflow section due to natural advection. An air lift pump device J is provided in the tank first chamber E1 (T1) , and a lid also serves as a constant head storage tank for temporarily storing the water to be treated pumped up by the air lift pump device J and as an air vent. A box-shaped constant head box 1 having no contact is provided with a double contact aeration tank first chamber and a second chamber E1.
(T1), provided at a position higher than the liquid level of E2 (T2) ,
The fixed head box 1 has a downstream overflow portion 1a having a V notch formed in the middle partition 1d and a dropout 1
c and the treated water is contacted via the second chamber E2 (T
A discharge path H for discharging is provided in 2) . The air lift pump device J has a hollow pipe formed in a J-shape, and the upper end of an air lift air supply pipe 2 formed with an opening serving as an air supply portion K to the air lift pump device J at the lower end. The air supply pipe 3 is connected to the air supply pipe 3 via a flexible hose 4, and the air lift air supply pipe 2 is vertically movably inserted from the upper part of the air lift pump device J, and the contact aeration tank first chamber E 1 (T 1 A) a float L serving as a liquid level detecting means for detecting the liquid level, and the float L being rigidly connected to the air supply pipe 2; Interlocking means for interlocking K up and down is configured. In the constant head box 1, an overflow portion 1b formed by horizontally cutting an upper portion of a side wall 1e on the side of the first chamber E1 (T1) of the contact aeration tank is slightly higher than the overflow portion 1a to the downstream side. Even if the flow rate of the water to be treated pumped by the air lift pump device J becomes too large, the flow rate to the downstream side can be maintained substantially constant by overflowing from the overflow section 1b, A gutter-shaped return path B for returning the water to be treated that has overflowed from the overflow section 1b to the first anaerobic filter bed tank N1 is provided. In addition, even if the posture of the septic tank is slightly deviated during installation, for example, the return path B
The upper part of the air lift pump device J is made of a flexible pipe so that the inclination of the air lift pump device J can be easily and appropriately corrected. or,
For example, even if the inflow of the water to be treated into the septic tank stops for a relatively long time, even if the contact aeration tank first chamber E1 (T
The suction port J1 of the air lift pump device J is provided at the height of the control lower limit of the liquid level so that the liquid level in 1) does not drop too much. With the above configuration, for example, even if there is some variation in the amount of inflow of the water to be treated into the septic tank, or even if the pumping amount of the air lift pump device J is set slightly larger, the average flow rate is substantially constant. Thus, the water to be treated can be sent to the treatment tank on the downstream side, so that it is possible to provide a purification tank capable of performing stable biological treatment while being easy to maintain. The air lift pump device may be installed in the anaerobic filter bed tank second chamber N2 or the like.

【0008】〔別実施例〕 前記フロートLの代わりに、例えば圧力センサーを用い
た液面検出手段Lを用い、この検出結果に基づき、前記
液面の上下に追従して前記エアー供給部Kを上下に機械
的に駆動させる装置を設ける等、別の構成にしてもよ
い。
[Another embodiment] Instead of the float L, for example, a liquid level detecting means L using a pressure sensor is used, and based on the detection result, the air supply unit K follows the liquid level up and down. Another configuration may be adopted, such as providing a device that drives mechanically up and down.

【0009】尚、実用新案登録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
本考案は添付図面の構成に限定されるものではない。
In the claims of the utility model registration, reference numerals are written for convenience of comparison with the drawings, but the present invention is not limited to the configuration of the attached drawings by the entry.

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

【図1】本考案による実施例における浄化槽の全体を示
す側断面図
FIG. 1 is a side sectional view showing an entire septic tank according to an embodiment of the present invention.

【図2】実施例の要部平面図FIG. 2 is a plan view of a main part of the embodiment.

【図3】実施例の要部側断面図FIG. 3 is a side sectional view of a main part of the embodiment.

【符号の説明】T1 上流側の処理槽 T2 下流側の処理槽 J エアーリフトポンプ装置 L 液面検出手段 K エアー供給部[Description of Signs ] T1 Upstream processing tank T2 Downstream processing tank J Air lift pump device L Liquid level detecting means K Air supply unit

───────────────────────────────────────────────────── フロントページの続き (72)考案者 原田 大 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)考案者 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 (56)参考文献 特開 平2−108900(JP,A) 特開 昭54−26509(JP,A) (58)調査した分野(Int.Cl.6,DB名) C02F 3/00 F04F 1/18──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor: Dai Harada 2 at Takamatsu, Kosai-cho, Koga-gun, Shiga Prefecture Inside the Kubota Shiga Plant (72) Inventor: Kazuyuki Honda 2nd Takamatsu, Kosai-cho, Koga-gun, Shiga 1 Kubota Corporation Shiga Plant (56) References JP-A-2-108900 (JP, A) JP-A-54-26509 (JP, A) (58) Fields investigated (Int. Cl. 6 , DB name) ) C02F 3/00 F04F 1/18

Claims (1)

(57)【実用新案登録請求の範囲】(57) [Scope of request for utility model registration] 【請求項1】 複数の処理槽(T1,T2)を流路方向
に直列に設けた浄化槽であって、隣接する前記処理槽
(T2)の上流側の前記処理槽(T1)内にエアーリフ
トポンプ装置(J)を設けると共に、そのエアーリフト
ポンプ装置(J)を、一端側を上方に開口するととも
に、揚水した被処理水を下流側の前記処理槽(T2)
排出する排出路(H)に接続自在に形成し、他端側を
流側の前記処理槽(T1)内に開口させてあるU字管を
設けるとともに、その排出路の下流側に前記エアーリフ
トポンプ装置(J)の被処理水を下流側に排出する落し
口(1c)を設け、かつ、前記一端側にエアーリフト用
エアー供給管(2)を挿入して、その開口部を前記U字
管とは独立して上下移動自在に形成してエアー供給部
(K)を設けて構成し、前記上流側の処理槽(T1)
液面を検出する液面検出手段(L)を設け、前記液面検
出手段(L)の検出結果に基づき、前記液面の上下に追
従して前記エアー供給部(K)を、前記落し口(1c)
に対して上下移動せて、上流側の処理槽の液面の上下変
動量の割合に対する移送流量の変動を小さくする連動手
段を設けてある浄化槽。
1. A purifying tank comprising a plurality of processing tanks (T1, T2) provided in series in a flow direction, wherein the adjacent processing tanks are provided.
An air lift pump device (J) is provided in the treatment tank (T1) on the upstream side of (T2) , and the air lift pump device (J) is opened at one end side and the water to be treated is pumped up. Is formed so as to be freely connectable to a discharge path (H) for discharging the processing tank (T2) on the downstream side, and the other end is upward.
Rutotomoni provided <br/> flow side the processing bath (T1) U-shaped tube which had been opened in the said downstream side of the discharge path Earifu
To discharge the water to be treated by the pump unit (J) to the downstream side
A port (1c) is provided, and an air supply pipe (2) for air lift is inserted into the one end , and the opening is formed so as to be vertically movable independently of the U-shaped pipe. (K), a liquid level detecting means (L) for detecting the liquid level of the upstream processing tank (T1) , and the liquid level detecting means (L) based on the detection result of the liquid level detecting means (L). The air supply unit (K) is moved up and down on the surface, and the air outlet (1c)
A purification tank provided with interlocking means for moving up and down with respect to the flow rate of the liquid flow in the upstream processing tank so as to reduce the fluctuation of the transfer flow rate with respect to the ratio of the vertical fluctuation amount of the liquid level in the upstream processing tank.
JP1991043893U 1991-06-12 1991-06-12 Septic tank Expired - Fee Related JP2587460Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1991043893U JP2587460Y2 (en) 1991-06-12 1991-06-12 Septic tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1991043893U JP2587460Y2 (en) 1991-06-12 1991-06-12 Septic tank

Publications (2)

Publication Number Publication Date
JPH04137799U JPH04137799U (en) 1992-12-22
JP2587460Y2 true JP2587460Y2 (en) 1998-12-16

Family

ID=31924150

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1991043893U Expired - Fee Related JP2587460Y2 (en) 1991-06-12 1991-06-12 Septic tank

Country Status (1)

Country Link
JP (1) JP2587460Y2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4702750B2 (en) * 2006-07-07 2011-06-15 株式会社ハウステック Water treatment equipment

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5426509A (en) * 1977-07-29 1979-02-28 Matsushita Electric Works Ltd Air lift pump
JPH02108900A (en) * 1988-10-15 1990-04-20 Matsushita Electric Works Ltd Pumping device in sewage disposal
JPH0647598Y2 (en) * 1988-10-26 1994-12-07 松下電工株式会社 Sewage treatment equipment
JPH02290296A (en) * 1989-01-14 1990-11-30 Matsushita Electric Works Ltd Sewage treatment apparatus

Also Published As

Publication number Publication date
JPH04137799U (en) 1992-12-22

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