JPH11104664A - Septic tank - Google Patents

Septic tank

Info

Publication number
JPH11104664A
JPH11104664A JP26597897A JP26597897A JPH11104664A JP H11104664 A JPH11104664 A JP H11104664A JP 26597897 A JP26597897 A JP 26597897A JP 26597897 A JP26597897 A JP 26597897A JP H11104664 A JPH11104664 A JP H11104664A
Authority
JP
Japan
Prior art keywords
tank
water
filter bed
lift pump
air lift
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
JP26597897A
Other languages
Japanese (ja)
Inventor
Takashi Kowada
孝 小和田
Atsushi Hibino
淳 日比野
Tsutomu Ishigaki
力 石垣
Yuji Koizumi
裕二 小泉
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.)
Showa Denko Materials Co Ltd
Original Assignee
Hitachi 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 Hitachi Chemical Co Ltd filed Critical Hitachi Chemical Co Ltd
Priority to JP26597897A priority Critical patent/JPH11104664A/en
Publication of JPH11104664A publication Critical patent/JPH11104664A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide a septic tank capable of easily adjusting the amt. of circulating water without using a distributing and metering device. SOLUTION: A septic tank is partitioned by a partition wall so that an anaerobic filter bed tank, an aerobic filter bed tank, a treated water tank or a sedimentation tank and a disinfection tank are arranged in this order from an upstream side and constituted so as to circulate a part of water in the aerobic filter bed tank and the treated water tank or the sedimentation tank to the anaerobic filter bed tank. In this case, a transfer device circulating the water in the aerobic filter bed tank and the treated water tank or the sedimentation tank to the anaerobic filter bed tank is an air lift pump system and an adjusting valve 31 for adjusting a water pumping-up amt. and the transfer pipe 21 communicating with an air lift pump 11 to transfer the pumped-up water in the tanks to the anaerobic filter bed tank are arranged to the air lift pump 11 and a standard line 22 of a circulating amt. of water is provided to the outflow opening part of the transfer pipe 21 and the air lift pump 11 is operated to transfer pumped-up circulating water to the anaerobic filter bed tank.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、家庭雑排水及びし
尿を処理する汚水浄化槽であって、特には槽内水の移行
装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a sewage treatment tank for treating domestic wastewater and night soil, and more particularly to a device for transferring water in the tank.

【0002】[0002]

【従来の技術】従来から用いられてきた汚水浄化槽につ
いて、図4を用いて説明すると汚水浄化槽1は、仕切壁
2、3、4、5にて仕切られ、上流側から嫌気濾床槽第
1室6、嫌気濾床槽第2室7、好気濾床槽8、処理水槽
9(沈殿槽の場合もある)、消毒槽10の順に配列され
ている。そして、処理水質の安定化及び窒素除去のため
に、処理水槽9の槽内水をエアリフポンプ11により吸
い上げ、嫌気濾床槽第1室6へ循環(返送)させてい
る。尚、循環させるのは、図4に示すような処理水槽9
の槽内水に限定されるものではなく、他に好気濾床槽8
又は沈殿槽の槽内水の場合もある。
2. Description of the Related Art A conventional sewage purifying tank will be described with reference to FIG. 4. A sewage purifying tank 1 is divided by partition walls 2, 3, 4, and 5, and a first anaerobic filter tank is provided from an upstream side. A chamber 6, an anaerobic filter bed second chamber 7, an aerobic filter bed tank 8, a treatment water tank 9 (sometimes a sedimentation tank), and a disinfection tank 10 are arranged in this order. Then, in order to stabilize the quality of the treated water and remove nitrogen, the water in the treated water tank 9 is sucked up by an air lift pump 11 and circulated (returned) to the first chamber 6 of the anaerobic filter bed tank. It is to be noted that the circulation is performed in the treatment water tank 9 as shown in FIG.
The water in the tank is not limited to the aerobic filter tank 8
Alternatively, the water in the sedimentation tank may be used.

【0003】前記処理水槽9から嫌気濾床槽第1室6へ
循環させる水量は、極めて少ない(数リットル/分)た
め、市販の水中ポンプが使用できず、図4(b)に示す
ように空気を推進力とするエアリフポンプ11を使用し
て、揚水し循環している。
[0003] Since the amount of water circulated from the treatment water tank 9 to the first anaerobic filter bed tank 6 is extremely small (several liters / minute), a commercially available submersible pump cannot be used, and as shown in FIG. Water is pumped and circulated using an air riff pump 11 that uses air as a driving force.

【0004】エアリフトポンプ11は、図5に示すとお
り、その上部に循環水量を調整する分配計量装置12が
設置されている。エアリフトポンプ11の揚水の仕組み
は、内管13より送風した空気14をその底部から吐出
させ、外管15と内管13との間を上昇する際に、前記
外管15外部の槽内水16を吸引して分配計量装置12
に揚水するようにしている。
As shown in FIG. 5, a distribution metering device 12 for adjusting the amount of circulating water is installed on the upper part of the air lift pump 11. The water pumping mechanism of the air lift pump 11 discharges the air 14 blown from the inner pipe 13 from the bottom thereof and raises the air 14 between the outer pipe 15 and the inner pipe 13. Suction and dispensing and weighing device 12
So that the water is pumped.

【0005】分配計量装置12は、循環水17を計量す
る三角堰18と循環水量を調整する戻り堰19から形成
される。槽内水16はエアリフトポンプ11により過剰
に揚水され、必要な循環水量のみを三角堰18から越流
させる。前記循環水量の調整は戻り堰19の高さを変化
させることにより行い、余剰水20は戻り堰19から越
流させ、揚水した元の槽に戻すものである。
[0005] The distribution metering device 12 is formed of a triangular weir 18 for measuring circulating water 17 and a return weir 19 for adjusting the amount of circulating water. The in-tank water 16 is pumped excessively by the air lift pump 11, and only the required amount of circulating water overflows from the triangular weir 18. The adjustment of the amount of circulating water is performed by changing the height of the return weir 19, and the surplus water 20 is caused to overflow from the return weir 19 and return to the original tank that has been pumped.

【0006】[0006]

【発明が解決しようとする課題】従来技術において、槽
内水16を過剰に揚水する目的は、必要水量のみを揚水
する場合、外管15と内管13との隙間幅を変化させ、
即ち抵抗を変えることにより揚水量を調整する必要があ
るが、循環水量が数リットル/分のような少ないレベル
では、この隙間幅が著しく小さくなるために、汚泥など
により隙間が部分的に閉塞して揚水ができないといった
現象を避けるためである。
In the prior art, the purpose of excessively pumping the water 16 in the tank is to change the gap width between the outer pipe 15 and the inner pipe 13 when pumping only the required amount of water.
That is, it is necessary to adjust the pumping amount by changing the resistance. However, at a small level such as several liters / minute, the gap width becomes extremely small, so that the gap is partially closed by sludge or the like. This is to avoid the phenomenon that pumping is not possible.

【0007】そのため、前述したような分配計量装置1
2をエアリフトポンプ11に設置して対応している。し
かし、循環水量の設定は戻り堰19の高さの微調整と三
角堰18から越流する循環水17を容器を用いて測定し
つつ行うため、大変煩雑な作業である。又、前記戻り堰
19の高さの微調整ができたとしても、三角堰18及び
戻り堰19には汚泥が付着しやすく、汚泥の付着量によ
り各堰の高さも変化してしまうために、結果として循環
水量が初期設定と異なり、安定した移行ができないとい
った課題がある。
[0007] Therefore, the dispensing and weighing device 1 as described above.
2 is installed in the air lift pump 11 to cope with it. However, the setting of the amount of circulating water is a very complicated operation because the setting of the height of the return weir 19 and the measurement of the circulating water 17 flowing from the triangular weir 18 using a container are performed. Further, even if the height of the return weir 19 can be finely adjusted, sludge easily adheres to the triangular weir 18 and the return weir 19, and the height of each weir changes depending on the amount of sludge attached. As a result, there is a problem that the circulating water amount is different from the initial setting, and a stable shift cannot be performed.

【0008】本発明は、以上のような課題に鑑み、従来
から使用している分配計量装置12を不要とするととも
に、数リットル/分程度の少ない循環水の流量調整を容
易に行いえる移行装置を内臓した汚水浄化槽を提供する
ことを目的とする。
In view of the above-mentioned problems, the present invention eliminates the need for the conventional dispensing and measuring device 12 and makes it possible to easily adjust the flow rate of the circulating water as low as several liters / minute. It is an object of the present invention to provide a sewage septic tank incorporating the same.

【0009】[0009]

【課題を解決するための手段】本発明は、図3に示すよ
うに、槽内を仕切壁2、3、4、5で仕切り、上流側か
ら嫌気濾床槽、好気濾床槽8、処理水槽9又は沈殿槽、
消毒槽10の順に配列し、且つ、好気濾床槽8、処理水
槽9又は沈殿槽の槽内水の一部を前記嫌気濾床槽へと循
環させる浄化槽において、前記好気濾床槽8、処理水槽
9又は沈殿槽の槽内水を嫌気濾床槽へ循環する移行装置
がエアリフトポンプ方式であって、詳しくは図1及び図
2に示すように、該エアリフトポンプ11に揚水量を調
整する調整弁31と、該エアリフトポンプ11に連通
し、前記揚水した槽内水16を嫌気濾床槽へ移行する移
行管21とを設置し、該移行管21の流出側開口部に循
環水量の目安線22を設けたことを特徴とする。
According to the present invention, as shown in FIG. 3, the inside of the tank is partitioned by partition walls 2, 3, 4, and 5, and an anaerobic filter tank, an aerobic filter tank 8, Treated water tank 9 or sedimentation tank,
In the purification tank which is arranged in the order of the disinfecting tank 10 and circulates a part of the water in the aerobic filter bed tank 8, the treatment water tank 9 or the sedimentation tank to the anaerobic filter bed tank, The transfer device that circulates the water in the treatment water tank 9 or the sedimentation tank to the anaerobic filter bed tank is an air lift pump system. Specifically, as shown in FIG. 1 and FIG. And a transfer pipe 21 that communicates with the air lift pump 11 and transfers the pumped water 16 from the tank to the anaerobic filter bed tank. It is characterized in that a reference line 22 is provided.

【0010】即ち、前記エアリフトポンプ11の揚水量
の調整は、揚水の推進力となる空気量を調整する弁31
によって行い、且つ、移行する循環水量の測定は移行管
21の流出側開口部に設けた目安線22で行い、揚水し
た循環水17を嫌気濾床槽へ移行するものである。
That is, the amount of water pumped by the air lift pump 11 is adjusted by adjusting the amount of air used as a driving force of the pump.
The measurement of the amount of circulating water to be transferred is performed by the reference line 22 provided at the outlet side opening of the transfer pipe 21, and the pumped circulating water 17 is transferred to the anaerobic filter bed tank.

【0011】尚、前記循環水17は、嫌気濾床槽へ循環
させるものであるが、嫌気濾床槽を図3に示すように複
数設けた場合には、処理時間を長くできるように、流入
口26に最も近い嫌気濾床槽第1室6へ循環させること
が好ましい。
The circulating water 17 is circulated to the anaerobic filter bed tank. If a plurality of anaerobic filter bed tanks are provided as shown in FIG. It is preferable to circulate to the anaerobic filter bed first chamber 6 closest to the inlet 26.

【0012】[0012]

【発明の実施の形態】エアリフトポンプ11の揚水量
は、水面とエアリフトポンプ11の下端との浸漬深さ、
管径、揚程及び空気量で決定されるが、本発明で対象と
しているのはその揚水量が数リットル/分程度の極めて
少ないレベルである。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The amount of water pumped by the air lift pump 11 is determined by the immersion depth between the water surface and the lower end of the air lift pump 11,
It is determined by the pipe diameter, the head, and the amount of air, but the present invention is directed to an extremely low level of about several liters / minute of pumped water.

【0013】そこで、エアリフトポンプの管路で汚泥が
付着しない空気配管路に、必要とする揚水量に見合った
空気量が挿入できる調整弁31を設け、揚水した循環水
は全量を移行するようにしている。更に、揚水した循環
水量の測定は、エアリフトポンプ11と連通する移行管
21の流出側開口部に設けた目安線22(図2参照)で
行うようにしている。
In view of this, an adjustment valve 31 is provided in the air pipe line to which sludge does not adhere in the pipe line of the air lift pump so that an air amount corresponding to a required pumping amount can be inserted, so that the entire amount of pumped circulating water is transferred. ing. Furthermore, the measurement of the amount of circulating water that is pumped is performed using a reference line 22 (see FIG. 2) provided at the outlet side opening of the transition pipe 21 that communicates with the air lift pump 11.

【0014】特に移行管21の流出側開口部に設ける目
安線22は、図2に示すように必要とする循環水量に見
合った目安線22を複数設けることで、処理規模が異な
っても空気量の調整を容易ならしめる。
In particular, as shown in FIG. 2, by providing a plurality of reference lines 22 corresponding to the required amount of circulating water, as shown in FIG. Makes adjustment easier.

【0015】また、エアリフトポンプ11と連通する移
行管21の流出側開口部は、水平方向の管径が垂直方向
の管径より短い筒状にすることで、水量の変化が水位変
化として容易に現出し読み取りやすいようにしてある。
したがって、前述した移行管21の流出側開口部は垂直
方向断面において縦長の楕円形状となるが、より水量の
変化が水位変化として容易に現出し読み取りやすいよう
に、図2(c)に示すとおり、楕円面に対して下側が管
底を頂点とする三角形状、もしくはそれに近似した形状
であってもよい。
The outlet side opening of the transition pipe 21 communicating with the air lift pump 11 has a tubular shape in which the horizontal pipe diameter is shorter than the vertical pipe diameter. Appears to be easy to read.
Therefore, the outflow-side opening of the above-mentioned transition pipe 21 has a vertically long elliptical shape in a vertical cross section, but as shown in FIG. Alternatively, the lower side of the elliptical surface may be a triangular shape having the tube bottom as the vertex, or a shape similar thereto.

【0016】[0016]

【実施例】以下、本発明の実施例について図面に沿って
説明する。図3に示す汚水浄化槽1は、その槽内を仕切
壁2、3、4、5で仕切り、上流側から嫌気濾床槽第1
室6、嫌気濾床槽第2室7、好気濾床槽8、処理水槽
9、消毒槽10の順に配置している。前記嫌気濾床槽第
1室6及び嫌気濾床槽第2室7には、濾材23、24が
設けられており、好気濾床槽8には微生物付着体25が
設けられている。
Embodiments of the present invention will be described below with reference to the drawings. In the sewage purification tank 1 shown in FIG. 3, the inside of the tank is partitioned by partition walls 2, 3, 4, and 5, and an anaerobic filter bed tank 1 is provided from the upstream side.
A chamber 6, an anaerobic filter bed second chamber 7, an aerobic filter bed tank 8, a treatment water tank 9, and a disinfection tank 10 are arranged in this order. The anaerobic filter tank first chamber 6 and the anaerobic filter tank second chamber 7 are provided with filter media 23 and 24, and the aerobic filter tank 8 is provided with a microorganism adherent 25.

【0017】流入口26から嫌気濾床槽第1室6に流入
した汚水27は、嫌気濾床槽第2室7、好気濾床槽8を
経て処理され、さらに処理水槽9を経て消毒槽10で滅
菌され、流出口28から処理水29として系外に放流さ
れる。処理水槽9の槽内水の一部は、処理水質の安定化
と脱窒のためにエアリフトポンプ11により揚水され、
移行管21によって、嫌気濾床槽第1室6へ循環(返
送)される。
The sewage 27 flowing into the first anaerobic filter tank 6 from the inlet 26 is treated through the second anaerobic filter tank 7 and the aerobic filter tank 8, and further through the treated water tank 9 to the disinfecting tank. It is sterilized at 10 and discharged from the outlet 28 as treated water 29 outside the system. Part of the water in the treatment water tank 9 is pumped by an air lift pump 11 for stabilization of treatment water quality and denitrification,
The transfer pipe 21 circulates (returns) the anaerobic filter bed tank 1 to the first chamber 6.

【0018】エアリフトポンプ11及び移行管21につ
いて、図1を使用し詳細に述べると、ブロワ30から調
整弁31を介してエアリフトポンプ11へ挿入された空
気14は、内管13の下端から吐出され外管15と前記
内管13の間を上昇する。前記空気14が上昇する推進
力は、槽内水16を揚水させ、前記揚水は移行管21か
ら循環水17として嫌気濾床槽第1室6へ至る。
The air lift pump 11 and the transfer pipe 21 will be described in detail with reference to FIG. 1. Air 14 inserted into the air lift pump 11 from the blower 30 via the regulating valve 31 is discharged from the lower end of the inner pipe 13. It rises between the outer tube 15 and the inner tube 13. The propulsion force by which the air 14 rises causes the tank water 16 to be pumped, and the pumping water reaches the anaerobic filter bed tank 1 chamber 6 as the circulating water 17 from the transition pipe 21.

【0019】循環水量の測定及び調整は図2を使用して
詳細に述べると、循環水17は移行管21の流出側開口
部から流出されるが、その循環水量は前記流出側開口部
(イ部、図1参照)の管内に設けた循環水目安線22で
測定することができる。即ち、予め水量と水位高さとの
関係を測定しておき、その高さを循環水目安線22とし
ておけば、循環水量が判るものである。また、循環水量
の調整は必要とする循環水目安線22になるように、前
記した調整弁31を用いて空気量を変えることで設定で
きる。
The measurement and adjustment of the amount of circulating water will be described in detail with reference to FIG. 2. The circulating water 17 flows out of the outlet side opening of the transition pipe 21. (See FIG. 1, FIG. 1). That is, if the relationship between the water amount and the water level height is measured in advance and the height is set as the circulating water reference line 22, the circulating water amount can be determined. Adjustment of the amount of circulating water can be set by changing the amount of air using the above-described adjusting valve 31 so that the required circulating water reference line 22 is obtained.

【0020】循環水量は、移行管21の流出側開口部
(イ部)において、図2(b)に示すように、水平方向
の管径が垂直方向の管径より短い筒状、即ち、垂直方向
断面において縦長の楕円形状としており、水量の変化が
水位変化として大きく現出するため、容易に測定及び調
整ができる。又、図2(c)に示すように、楕円面に対
して下側が管底を頂点とする三角形状であれば、更に精
度よく測定及び調整ができる。
As shown in FIG. 2 (b), the amount of circulating water at the outflow opening (portion a) of the transition pipe 21 is cylindrical, that is, the pipe diameter in the horizontal direction is shorter than the pipe diameter in the vertical direction. It has a vertically long elliptical shape in the cross section in the direction, and a change in the amount of water appears largely as a change in water level, so that measurement and adjustment can be easily performed. Further, as shown in FIG. 2 (c), if the lower side of the elliptical surface is a triangular shape having the tube bottom as the apex, measurement and adjustment can be performed with higher accuracy.

【0021】[0021]

【発明の効果】以上説明したとおり、本発明によれば、
従来分配計量装置を使用していたために、循環水量の調
整が困難であったが、空気量を変化させる調整弁と移行
管の流出側開口部に循環水目安線を設けることにより、
分配計量装置を用いることなく、容易に流量調整を行う
ことが可能となる。又、移行管の流出側開口部の形状を
水平方向の管径が垂直方向の管径より短いものを使用す
ることで、より精度よく流量調整を行うことができる。
As described above, according to the present invention,
Conventionally, it was difficult to adjust the amount of circulating water due to the use of a dispensing and metering device.However, by providing a regulating valve for changing the amount of air and a circulating water guide line at the outlet side opening of the transition pipe,
The flow rate can be easily adjusted without using a distributing and weighing device. In addition, the flow rate can be adjusted more accurately by using a shape of the outlet side opening of the transition pipe whose horizontal diameter is shorter than vertical diameter.

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

【図1】本発明の要部であるエアリフトポンプ及び移行
管の斜視図を示す。
FIG. 1 shows a perspective view of an air lift pump and a transition pipe which are main parts of the present invention.

【図2】本発明に用いる移行管の流出側開口部を示す図
面であり、(a)は、図1のイ部拡大図を示し、(b)
及び(c)は、(a)のA−A断面図を示す。
FIGS. 2A and 2B are diagrams showing an outlet side opening of a transition pipe used in the present invention, wherein FIG. 2A is an enlarged view of a portion a in FIG. 1 and FIG.
(C) shows an AA sectional view of (a).

【図3】本発明の実施例を示す汚水浄化槽であり、
(a)は水平方向断面図を示し、(b)は、(a)のA
−A断面図を示す。
FIG. 3 is a sewage purification tank showing an embodiment of the present invention,
(A) shows a horizontal cross-sectional view, and (b) shows A in (a).
FIG.

【図4】従来例を示す汚水浄化槽であり、(a)は水平
方向断面図を示し、(b)は、(a)のA−A断面図を
示す。
FIG. 4 is a sewage purification tank showing a conventional example, in which (a) shows a horizontal sectional view, and (b) shows an AA sectional view of (a).

【図5】従来、使用されていた分配計量装置の斜視図を
示す。
FIG. 5 is a perspective view of a conventional dispensing and weighing device.

【符号の説明】[Explanation of symbols]

1.汚水浄化槽 2.仕切壁 3.仕切壁 4.仕切壁
5.仕切壁 6.嫌気濾床槽第1室 7.嫌気濾床槽
第2室 8.好気濾床槽 9.処理水槽 10.消毒槽
11.エアリフトポンプ 12.分配計量装置 1
3.内管 14.空気 15.外管 16.槽内水 1
7.循環水 18.三角堰 19.戻り堰 20.余剰水 21.移行管 22.循環水目安線 2
3.濾材 24.濾材 25.微生物付着体 26.流入口 27.汚水 2
8.流出口 29.処理水 30.ブロワ 31.調整弁
1. Sewage septic tank 2. Partition wall 3. Partition wall 4. Partition wall 5. Partition wall 6. Anaerobic filter tank 1st room 7. 7. Anaerobic filter tank 2nd room Aerobic filter bed tank 9. Treatment water tank 10. Disinfection tank 11. Air lift pump 12. Dispensing and weighing device 1
3. Inner pipe 14. Air 15. Outer tube 16. Water in tank 1
7. Circulating water 18. Triangular weir 19. Return weir 20. Surplus water 21. Transition pipe 22. Circulating water guide line 2
3. Filter medium 24. Filter medium 25. Microbial adherent 26. Inlet 27. Sewage 2
8. Outlet 29. Treated water 30. Blower 31. tuning valve

───────────────────────────────────────────────────── フロントページの続き (72)発明者 小泉 裕二 茨城県下館市大字下江連1250番地 日立化 成工業株式会社結城工場内 ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Yuji Koizumi 1250 Shimoedori, Shimodate-shi, Ibaraki Pref.Hitachi Chemical Industry Co., Ltd.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 槽内を仕切壁で仕切り、上流側から嫌気
濾床槽、好気濾床槽、処理水槽又は沈殿槽、消毒槽の順
に配列し、且つ、好気濾床槽、処理水槽又は沈殿槽の槽
内水の一部を前記嫌気濾床槽へと循環させる浄化槽にお
いて、前記好気濾床槽、処理水槽又は沈殿槽の槽内水を
嫌気濾床槽へ循環する移行装置がエアリフトポンプ方式
であって、該エアリフトポンプに揚水量を調整する調整
弁と、該エアリフトポンプに連通し、前記揚水した槽内
水を嫌気濾床槽へ移行する移行管とを設置し、該移行管
の流出側開口部に循環水量の目安線を設けたことを特徴
とする汚水浄化槽。
A tank is partitioned by a partition wall, and an anaerobic filter bed tank, an aerobic filter bed tank, a treatment water tank or a sedimentation tank, and a disinfection tank are arranged in this order from the upstream side, and an aerobic filter bed tank and a treatment water tank are arranged. Alternatively, in a purification tank that circulates a part of the water in the sedimentation tank to the anaerobic filter bed tank, a transfer device that circulates the water in the aerobic filter bed tank, the treatment water tank or the sedimentation tank to the anaerobic filter bed tank is provided. An air lift pump system, comprising: an adjusting valve for adjusting the pumping amount of the air lift pump; and a transfer pipe communicating with the air lift pump and transferring the pumped water in the tank to an anaerobic filter bed tank. A sewage treatment tank characterized in that a guide line for the amount of circulating water is provided at the outlet of the pipe.
【請求項2】 エアリフトポンプに連通し、流出側開口
部に循環水量の目安線を設けた移行管が、流出側開口部
において水平方向の管径が、垂直方向の管径より短い筒
状体からなることを特徴とする請求項1記載の汚水浄化
槽。
2. A transfer pipe which communicates with an air lift pump and has a guide line for the amount of circulating water at an outlet side opening, wherein a tubular pipe having a horizontal pipe diameter shorter than a vertical pipe diameter at the outlet side opening. The sewage purification tank according to claim 1, comprising:
JP26597897A 1997-09-30 1997-09-30 Septic tank Pending JPH11104664A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP26597897A JPH11104664A (en) 1997-09-30 1997-09-30 Septic tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP26597897A JPH11104664A (en) 1997-09-30 1997-09-30 Septic tank

Publications (1)

Publication Number Publication Date
JPH11104664A true JPH11104664A (en) 1999-04-20

Family

ID=17424676

Family Applications (1)

Application Number Title Priority Date Filing Date
JP26597897A Pending JPH11104664A (en) 1997-09-30 1997-09-30 Septic tank

Country Status (1)

Country Link
JP (1) JPH11104664A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001329999A (en) * 2000-05-23 2001-11-30 Hitachi Chem Co Ltd Fluid transfer device
JP2012050955A (en) * 2010-09-03 2012-03-15 Fuji Clean Co Ltd Transfer pipe and device for treating waste water

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001329999A (en) * 2000-05-23 2001-11-30 Hitachi Chem Co Ltd Fluid transfer device
JP2012050955A (en) * 2010-09-03 2012-03-15 Fuji Clean Co Ltd Transfer pipe and device for treating waste water

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