JPH11104673A - Septic tank - Google Patents
Septic tankInfo
- Publication number
- JPH11104673A JPH11104673A JP26597797A JP26597797A JPH11104673A JP H11104673 A JPH11104673 A JP H11104673A JP 26597797 A JP26597797 A JP 26597797A JP 26597797 A JP26597797 A JP 26597797A JP H11104673 A JPH11104673 A JP H11104673A
- Authority
- JP
- Japan
- Prior art keywords
- tank
- water
- lift pump
- air lift
- filter bed
- 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.)
- Granted
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 66
- 238000005192 partition Methods 0.000 claims abstract description 10
- 238000004659 sterilization and disinfection Methods 0.000 claims abstract description 7
- 239000010865 sewage Substances 0.000 claims description 12
- 238000000746 purification Methods 0.000 claims description 5
- 238000004062 sedimentation Methods 0.000 claims description 5
- 238000011144 upstream manufacturing Methods 0.000 claims description 5
- 238000001556 precipitation Methods 0.000 abstract 2
- 238000005086 pumping Methods 0.000 description 17
- 239000010802 sludge Substances 0.000 description 6
- 238000005303 weighing Methods 0.000 description 4
- 239000000463 material Substances 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 230000007704 transition Effects 0.000 description 2
- 230000001464 adherent effect Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000010840 domestic wastewater Substances 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 230000001141 propulsive effect Effects 0.000 description 1
- 230000010349 pulsation Effects 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 230000000087 stabilizing effect Effects 0.000 description 1
Landscapes
- Treatment Of Biological Wastes In General (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、し尿及び家庭用排
水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 night soil and domestic wastewater, 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3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トポンプ11によ
り汲み上げ、嫌気濾床槽第1室6へ循環(返送)させて
いる。循環させるのは、図3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. 3. A sewage purifying tank 1 is divided by partition walls 2, 3, 4, and 5, and an anaerobic filter bed tank is provided from an upstream side. One chamber 6, anaerobic filter bed second chamber 7, aerobic filter bed tank 8, treated water tank 9 (sometimes a sedimentation tank), and 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 pumped up by the air lift pump 11 and circulated (returned) to the first chamber 6 of the anaerobic filter bed tank. Circulation is not limited to the water in the treatment water tank 9 as shown in FIG. 3, but may be the water in the aerobic filter bed tank 8 or the sedimentation tank.
【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、空気を推進力とす
るエアリフトポンプ11を使用して揚水し循環してい
る。Since the amount of water circulated from the treatment water tank 9 to the first chamber 6 of the anaerobic filter bed tank is extremely small (several liters / minute), a commercially available submersible pump cannot be used, and an air lift pump 11 using air as a driving force is used. Use pumping and circulating.
【0004】エアリフトポンプ11には、図4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より送風された空気14がその底部から
吐出され、外管15と内管13との間を上昇し、その際
に前記外管15外部の槽内水16も吸引されて分配計量
装置12に揚水されるようになっている。[0004] As shown in FIG. 4, a distribution metering device 12 for adjusting the amount of circulating water is provided above the air lift pump 11.
Is installed. The pumping mechanism of the air lift pump 11 is such that air 14 blown from the inner pipe 13 is discharged from the bottom and rises between the outer pipe 15 and the inner pipe 13, and at that time, the inside of the tank outside the outer pipe 15 The water 16 is also sucked and pumped to the distribution and metering device 12.
【0005】前記分配計量装置12は、循環水18を計
量する三角堰17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17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
から越流させて揚水した元の槽に戻すものである。[0005] The distribution metering device 12 comprises a triangular weir 17 for measuring circulating water 18 and a return weir 19 for adjusting the amount of circulating water. The water 16 in the tank is pumped excessively by the air lift pump 11, and only the necessary amount of circulating water flows from the triangular weir 17. The circulating water amount is adjusted by changing the height of the return weir 19, and the excess water 20
It is to return to the original tank that was overflowed and 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
り、移行水量が数リットル/分のような少ないレベルで
は、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 amount of pumped water by changing the resistance. At a low 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17から越流する循環水18を容器を用いて測定し
つつ行うため、著しく煩雑な作業となっている。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
17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, since the setting of the circulating water amount is performed while finely adjusting the height of the return weir 19 and measuring the circulating water 18 flowing from the triangular weir 17 using a container, the operation is extremely complicated. Also, even if the height of the return weir 19 can be finely adjusted, sludge easily adheres to the triangular weir 17 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を不要とすると共
に、数リットル/分程度の少ない循環水量の移行が安定
して行いえる移行装置を内蔵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 problems, the present invention eliminates the need for the conventional dispensing and metering device 12 and enables the transfer of a small amount of circulating water of several liters / minute to be performed stably. An object of the present invention is to provide a sewage septic tank incorporating a sewage treatment tank.
【0009】[0009]
【課題を解決するための手段】本発明は、図2及び図1
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の順に配列させた浄化槽において、
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、該エアリフトポンプ11の吸い込み口に、管内
を移動可能な開口を有する絞り部24を設けたことを特
徴とする。The present invention has been described with reference to FIGS.
As shown in, the inside of the tank is partitioned by partition walls 2, 3, 4, and 5,
In the purification tank arranged in the order of anaerobic filter bed tank, aerobic filter bed tank 8, treated water tank 9 or settling tank, and disinfection tank 10 from the upstream side,
The transfer device that circulates the water in the aerobic filter bed tank 8, the treatment water tank 9 or the sedimentation tank to the anaerobic filter bed tank is an air lift pump system, and can be moved in the pipe to the suction port of the air lift pump 11. It is characterized in that a diaphragm 24 having an opening is provided.
【0010】即ち、前記エアリフトポンプ11の吸い込
み口に、管内を移動でき開口を有する絞り部24を設
け、該絞り部24の開口の大きさで前記エアリフトポン
プ11の揚水量能力を決定し、且つ、管内に付着した汚
泥を前記絞り部24を動かして除去し、安定した揚水を
行い、揚水した水を嫌気濾床槽へ移行するものである。That is, a throttle 24 which can move in the pipe and has an opening is provided at the suction port of the air lift pump 11, and the pumping capacity of the air lift pump 11 is determined by the size of the opening of the throttle 24, and The sludge adhering to the inside of the pipe is removed by moving the squeezing section 24 to perform stable water pumping, and the pumped water is transferred to the anaerobic filter bed tank.
【0011】[0011]
【発明の実施の形態】エアリフトポンプ11の揚水量
は、水面とそ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。BEST MODE FOR CARRYING OUT THE INVENTION The amount of water pumped by an air lift pump 11 is determined by the immersion depth between the water surface and its lower end, the pipe diameter, the head, and the amount of air. It is an extremely small level of several liters / minute.
【0012】通常、エアリフトポンプは、揚水量が多い
領域で使用されるために、少揚水量の場合にはその調整
が容易ではない。そこで、エアリフトポンプ11自体に
は、過剰の揚水能力を持たせつつ、吸い込み口に絞り部
24(抵抗部)を設けることにより、目標の揚水量を得
るようにしている。[0012] Usually, the air lift pump is used in a region where the amount of pumped water is large. Therefore, when the amount of pumped water is small, its adjustment is not easy. Therefore, the air lift pump 11 itself is provided with a throttle portion 24 (resistance portion) at the suction port while having an excessive water pumping capacity, thereby obtaining a target water pumping amount.
【0013】絞り部24の開口径φDは任意に決定で
き、目標揚水量に合わせて個々に変化させるものであ
る。そして、絞り部24はエアリフトポンプ11の吸い
込み口に設けられ、該エアリフトポンプ11の内管13
と接続する支持材25によって懸垂される。ここで該支
持材25は、挿入する空気14の吐出と絞り部24を経
て上昇してくる槽内水16の揚水に律速とならないよう
に、絞り部24の開口径φDより大きい面積の通路を有
する形状としている。The opening diameter φD of the throttle unit 24 can be arbitrarily determined, and is individually changed in accordance with the target pumping amount. The throttle portion 24 is provided at a suction port of the air lift pump 11, and the inner pipe 13 of the air lift pump 11 is provided.
Suspended by a support member 25 connected to the Here, the support member 25 has a passage having an area larger than the opening diameter φD of the throttle unit 24 so that the discharge of the air 14 to be inserted and the pumping of the water 16 rising through the throttle unit 24 are not limited. Shape.
【0014】更に、本発明に用いるエアリフトポンプ1
1の構造において、絞り部24の開口径φDを一定とし
て揚水能力を低下させたい場合には、挿入する空気14
が内管13から外管15に向かって吐出する開放部、即
ち、前記空気14が内管13から吐出する開放部を水深
に対して、より浅い位置にすることで可能となる。Further, an air lift pump 1 used in the present invention
In the structure of FIG. 1, when it is desired to reduce the pumping capacity while keeping the opening diameter φD of the throttle unit 24 constant, the air
This can be achieved by setting the opening where the air 14 is discharged from the inner pipe 13 toward the outer pipe 15, that is, the opening where the air 14 is discharged from the inner pipe 13 at a shallower position relative to the water depth.
【0015】エアリフトポンプ11の内管13と外管1
5との間、又は、支持材25の通路、更には、絞り部2
4に汚泥が付着し槽内水の揚水に支障が出たときは、内
管13を上下に移動することで汚泥の剥離除去ができ
る。更には、内管13を引き上げれば、それと接続され
ている前記支持材25及び絞り部24も引き上げられる
ため、各部位を容易に清掃できる。これらの操作によっ
て、安定した揚水が長期に渡って行いえる。The inner pipe 13 and the outer pipe 1 of the air lift pump 11
5 or the passage of the support material 25,
When sludge adheres to 4 and hinders the pumping of water in the tank, the sludge can be separated and removed by moving the inner pipe 13 up and down. Further, when the inner tube 13 is pulled up, the support member 25 and the throttle portion 24 connected thereto are also pulled up, so that each part can be easily cleaned. By these operations, stable pumping can be performed for a long time.
【0016】揚水した槽内水は全量を嫌気濾床槽へ移行
させるが、図2に示すように、複数の嫌気濾床槽を有す
る場合には、処理時間を長くするために、流入口29に
最も近い嫌気濾床槽第1室6へ移行させることが好まし
い。The entire amount of the pumped water in the tank is transferred to the anaerobic filter bed tank. However, as shown in FIG. 2, when a plurality of anaerobic filter bed tanks are provided, the inflow port 29 is provided to increase the treatment time. Is preferably transferred to the first anaerobic filter tank 1 chamber 6 which is closest to the anaerobic filter tank.
【0017】[0017]
【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2に示す汚水浄化槽1は、その槽内を仕切
壁2、3、4、5にて仕切り、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21、22が
設けられており、好気濾床槽8には微生物付着体23が
設けられている。Embodiments of the present invention will be described below with reference to the drawings. The sewage purification tank 1 shown in FIG. 2 is partitioned by partition walls 2, 3, 4, and 5 from the upstream side, and the anaerobic filter tank first chamber 6, the anaerobic filter tank second chamber 7, the aerobic filter from the upstream side. The floor tank 8, the treatment water tank 9, and the 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 21 and 22, and the aerobic filter tank 8 is provided with a microorganism adhering body 23.
【0018】流入口29から嫌気濾床槽第1室6に流入
した汚水28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30から処理水31として系外に放流さ
れる。好気濾床槽8の底部から槽内水の一部は、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27によって、嫌気濾床槽第1室6へ
循環(返送)される。The sewage 28 flowing from the inlet 29 into the first anaerobic filter tank 6 is processed through the second anaerobic filter tank 7 and the aerobic filter tank 8, and further through the treated water tank 9 to the disinfection tank. It is sterilized at 10 and discharged out of the system as treated water 31 from an outlet 30. Part of the water in the tank from the bottom of the aerobic filter tank 8 is pumped up by the air lift pump 11 for stabilization of the treated water quality and denitrification, and is circulated to the first anaerobic filter tank 6 by the transfer pipe 27. (Returned).
【0019】エアリフトポンプ11について、図1
(a)を使用し詳細に述べると、前記エアリフトポンプ
11は処理水槽9に設置され、その底部は仕切壁4を貫
いて好気濾床槽8の底部と連通している。外部から挿入
された空気14は、内管13下端の吐出部26から吐出
され支持材25の通路を通り、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、好
気濾床槽8底部から該槽内水16を絞り部24及び支持
材25の通路を経て、外管15と内管13の間を上昇さ
せ揚水する。揚水された水は、移行管27から循環水1
8として嫌気濾床槽第1室6へ移行される。The air lift pump 11 is shown in FIG.
More specifically, using (a), the air lift pump 11 is installed in a treated water tank 9, and the bottom of the air lift pump 11 communicates with the bottom of the aerobic filter bed tank 8 through the partition wall 4. The air 14 inserted from the outside is discharged from the discharge portion 26 at the lower end of the inner tube 13 and passes through the passage of the support member 25, so that the outer tube 15 and the inner tube 13
Rise between. The propulsive force by which the air 14 rises raises water in the tank 16 from the bottom of the aerobic filter bed tank 8 through the squeezing section 24 and the passage of the supporting material 25 to rise between the outer pipe 15 and the inner pipe 13. . The pumped water is transferred from the transfer pipe 27 to the circulating water 1.
The process moves to the first anaerobic filter tank 6 as 8.
【0020】エアリフトポンプ11は、所定量以上の空
気を挿入すると、脈動がない安定した状態で揚水を行な
う性質があり、本発明においても必要以上の揚水能力を
得るように過剰の空気14を送りこんでいる。しかし、
前記エアリフトポンプ11の吸い込み部、即ち、外管1
5の下端には、予めφDの開口を有する絞り部24を内
管13に懸垂して設けているために、必要量の揚水を安
定して得ることができる。The air lift pump 11 has a property of pumping water in a stable state with no pulsation when air of a predetermined amount or more is inserted. In the present invention, too, the excess air 14 is fed so as to obtain a pumping capacity more than necessary. In. But,
The suction portion of the air lift pump 11, that is, the outer tube 1
At the lower end of 5, a throttle portion 24 having an opening of φD is previously suspended from the inner tube 13, so that a required amount of pumping water can be obtained stably.
【0021】図1(b)は、本発明の別の実施例である
エアリフトポンプ11であり、内管13に挿入する空気
14の吐出部26を内管13の下端より上側に設けた場
合を示す。即ち、挿入する空気14は、内管13の下端
より上側にある吐出部26から吐出されるようにしてあ
る。尚、支持材25を介して内管13に懸垂される絞り
部24は、内管13の下端から吐出する場合と同じ位置
に設けられる。FIG. 1B shows an air lift pump 11 according to another embodiment of the present invention, in which a discharge portion 26 of the air 14 inserted into the inner pipe 13 is provided above the lower end of the inner pipe 13. Show. That is, the air 14 to be inserted is discharged from the discharge portion 26 above the lower end of the inner tube 13. Note that the throttle portion 24 suspended from the inner tube 13 via the support member 25 is provided at the same position as when discharging from the lower end of the inner tube 13.
【0022】[0022]
【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、移行水量の調
整と安定性に課題があったが、開口を有する絞り部を移
動できるように配置することにより、分配計量装置を使
用することなく、少ない揚水量でも安定した移行を行な
うことが可能となった。As described above, according to the present invention,
Conventionally, the use of a dispensing and weighing device had a problem in adjusting and stabilizing the amount of transferred water, but by arranging the squeezing section having an opening so that it could be moved, it was possible to reduce It has become possible to make a stable transition even with the amount of pumped water.
【図1】本発明の要部であるエアリフトポンプであり、
(a)は断面図を示し、(b)は他の実施例の断面図を
示す。FIG. 1 is an air lift pump which is a main part of the present invention;
(A) shows a cross-sectional view, and (b) shows a cross-sectional view of another embodiment.
【図2】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. 2 is a sewage purification tank showing an embodiment of the present invention,
(A) shows a horizontal sectional view, (b) shows A-
FIG.
【図3】従来の汚水浄化槽を示す断面図である。FIG. 3 is a sectional view showing a conventional sewage purification tank.
【図4】従来使用されていた分配計量装置の斜視図であ
る。FIG. 4 is a perspective view of a conventionally used dispensing and weighing device.
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
7.三角堰 18.循環水 19.戻り堰 20.余剰水 21.濾材 22.濾材 23.微生物
付着体 24. 絞り部 25.支持材 26.吐出部 27.移行管 28.汚
水 29.流入口 30.流出口 31.処理水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. Triangular weir 18. Circulating water 19. Return weir 20. Surplus water 21. Filter medium 22. Filter medium 23. Microbial adherent 24. Restrictor 25. Support material 26. Discharge unit 27. Transition tube 28. Sewage 29. Inlet 30. Outlet 31. Treated water
Claims (1)
濾床槽、好気濾床槽、処理水槽又は沈殿槽、消毒槽の順
に配列させた浄化槽において、前記好気濾床槽、沈殿槽
又は処理水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
の吸い込み口に、管内を移動可能な開口を有する絞り部
を設けたことを特徴とする汚水浄化槽。1. A purification tank in which 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 an upstream side. The transfer device for circulating the water in the sedimentation tank or the treatment water tank to the anaerobic filter bed tank is an air lift pump system, and the suction port of the air lift pump is provided with a throttle unit having an opening movable in the pipe. Characterized sewage septic tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP26597797A JP3975373B2 (en) | 1997-09-30 | 1997-09-30 | Wastewater septic tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP26597797A JP3975373B2 (en) | 1997-09-30 | 1997-09-30 | Wastewater septic tank |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH11104673A true JPH11104673A (en) | 1999-04-20 |
| JP3975373B2 JP3975373B2 (en) | 2007-09-12 |
Family
ID=17424663
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP26597797A Expired - Fee Related JP3975373B2 (en) | 1997-09-30 | 1997-09-30 | Wastewater septic tank |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3975373B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105621840A (en) * | 2016-02-29 | 2016-06-01 | 沈阳建筑大学 | Pressure-difference-type green ecological septic tank and use method thereof |
-
1997
- 1997-09-30 JP JP26597797A patent/JP3975373B2/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105621840A (en) * | 2016-02-29 | 2016-06-01 | 沈阳建筑大学 | Pressure-difference-type green ecological septic tank and use method thereof |
| CN105621840B (en) * | 2016-02-29 | 2018-01-30 | 沈阳建筑大学 | A kind of differential green ecological septic tank and its application method |
Also Published As
| Publication number | Publication date |
|---|---|
| JP3975373B2 (en) | 2007-09-12 |
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