JP2839065B2 - Septic tank - Google Patents

Septic tank

Info

Publication number
JP2839065B2
JP2839065B2 JP22678593A JP22678593A JP2839065B2 JP 2839065 B2 JP2839065 B2 JP 2839065B2 JP 22678593 A JP22678593 A JP 22678593A JP 22678593 A JP22678593 A JP 22678593A JP 2839065 B2 JP2839065 B2 JP 2839065B2
Authority
JP
Japan
Prior art keywords
tank
water
air supply
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
JP22678593A
Other languages
Japanese (ja)
Other versions
JPH0780484A (en
Inventor
八郎 佐藤
良人 北井
正修 岩橋
和之 本田
勝己 浜田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kubota Corp
Original Assignee
Kubota Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Kubota Corp filed Critical Kubota Corp
Priority to JP22678593A priority Critical patent/JP2839065B2/en
Publication of JPH0780484A publication Critical patent/JPH0780484A/en
Application granted granted Critical
Publication of JP2839065B2 publication Critical patent/JP2839065B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Treatment Of Biological Wastes In General (AREA)
  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)

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、上流側から嫌気濾床
槽、好気濾床槽、沈殿槽を被処理水が自然移流によりこ
の順に流れるように設けるとともに、消毒槽を設け、前
記好気濾床槽への散気用の第1エア供給管と、下流側か
ら上流側へ被処理水を返送する返送管用の第2エア供給
管と、被処理水を前記沈殿槽から前記消毒槽に移送する
エアリフト管用の第3エア供給管とを連設してあり、各
エア供給管はブロワに接続してある浄化槽に関する。
The present invention provides an anaerobic filter tank, an aerobic filter tank, and a sedimentation tank from the upstream side so that water to be treated flows in this order by natural advection, and a disinfection tank is provided. A first air supply pipe for diffusing air to the filter bed tank, a second air supply pipe for returning water to be treated from the downstream side to the upstream side, and disinfecting tank for supplying the treated water from the settling tank to the disinfecting tank A third air supply pipe for an air lift pipe to be transferred to the air purifier is connected to a septic tank connected to a blower.

【0002】[0002]

【従来の技術】従来、このような浄化槽としては、前記
第1、第2、第3エア供給管を格別にブロワに接続し
て、エア供給によって生じた気泡が、浮力によって水中
を上昇する際の揚水効果(以下エアリフト効果と称す
る)を利用して、被処理水を返送または移送(以下移送
等と略称する)させることで、ポンプで揚水する様な場
合に比して、設備面での低コスト化を図ることが考えら
れており、このようなものにおいては第3エア供給管へ
は、連続的にエア供給することしか考えられていなかっ
た。
2. Description of the Related Art Conventionally, in such a septic tank, the first, second, and third air supply pipes are specially connected to a blower so that air bubbles generated by air supply rise in water due to buoyancy. The water to be treated is returned or transported (hereinafter abbreviated as transport, etc.) using the water pumping effect (hereinafter referred to as the air lift effect) of the equipment, so that compared with the case of pumping the water, It has been considered to reduce the cost. In such a case, only continuous air supply to the third air supply pipe has been considered.

【0003】[0003]

【発明が解決しようとする課題】上述のような浄化槽
は、揚水ポンプ等の大がかりな設備を用いることなく被
処理水の移送等が行え、設備面で低コストかつメンテナ
ンスが容易という利点をもつ。一方、一般に散気用に供
給するエア供給量は、40〜80リットル/分であり、
返送管に供給するエア量は10〜15リットル/分であ
るのに対して、沈殿槽から、消毒槽に移送するエアリフ
ト管用のエア供給量は、10リットル/分以下(具体的
には従来2リットル/分で行われていた)の少ないエア
供給量であり、一定の流量を常時保つために、前記少な
いエア供給量を保持すると、浄化槽に流入する原水の流
量の変化に伴って、沈殿槽から消毒槽に移送される被処
理水の移送量が大きく変化する。
The above-mentioned septic tank has the advantage that the water to be treated can be transferred without using a large-scale facility such as a water pump and the like, and the facility is low in cost and easy to maintain. On the other hand, the air supply amount generally supplied for aeration is 40 to 80 liters / minute,
While the amount of air supplied to the return pipe is 10 to 15 liters / minute, the amount of air supplied to the air lift pipe from the sedimentation tank to the disinfection tank is 10 liters / minute or less (specifically, 2 to 15 liters / minute). Liter / min), and when the small air supply is maintained in order to always maintain a constant flow rate, the sedimentation tank is changed according to the change in the flow rate of the raw water flowing into the purification tank. The transfer rate of the water to be transferred transferred from the tank to the disinfection tank changes greatly.

【0004】そのため、原水が急激に流入した場合等、
浄化槽の水位が変動すると、沈殿槽から消毒槽に移送さ
れる被処理水の移送量が多くなり、充分に処理されてい
ない被処理水が放流される危険性があった。また、一度
に大量の被処理水が移送されると沈殿槽内に浮遊する汚
泥等(以下剥離汚泥と称する)が処理水とともに放流さ
れるおそれがあった。
[0004] Therefore, when raw water suddenly flows in,
When the water level in the septic tank fluctuates, the transfer amount of the water to be treated transferred from the sedimentation tank to the disinfection tank increases, and there is a risk that the water to be treated that is not sufficiently treated is discharged. Further, when a large amount of water to be treated is transferred at a time, sludge floating in the sedimentation tank (hereinafter referred to as separated sludge) may be discharged together with the treated water.

【0005】そこで本発明の目的は、上記実情に鑑み、
浄化槽外への処理水の放流量が大幅に変動することな
く、かつ、剥離汚泥が処理水に混入して放流されるおそ
れが少ない浄化槽を、低コストで提供する事にある。
Accordingly, an object of the present invention is to provide
An object of the present invention is to provide a septic tank at a low cost, in which the discharge flow rate of the treated water to the outside of the septic tank does not largely fluctuate and there is little possibility that the separated sludge is mixed with the treated water and discharged.

【0006】[0006]

【課題を解決するための手段】この目的を達成するため
の本発明の特徴構成は、好気濾床槽への散気用の第1エ
ア供給管と、下流側から上流側へ被処理水を返送する返
送管用の第2エア供給管と、被処理水を前記沈殿槽から
前記消毒槽に移送するエアリフト管用の第3エア供給管
とを一つのブロワに接続するとともに、前記ブロワから
第3エア供給管へ、エアを間欠的に供給可能にするため
のエア供給量調節手段を設けたことにあり、その作用効
果は以下の通りである。
To achieve the above object, the present invention is characterized by a first air supply pipe for diffusing air into an aerobic filter bed tank, and a treatment water flowing from a downstream side to an upstream side. And a third air supply pipe for an air lift pipe for transferring treated water from the sedimentation tank to the disinfection tank are connected to one blower, and the third air supply pipe is connected to the third blower from the blower. An air supply amount adjusting means for intermittently supplying air to the air supply pipe is provided, and the operation and effect thereof are as follows.

【0007】[0007]

【作用】つまり、第1、第2、第3エア供給管が一つの
ブロワに接続してあるから、ポンプ等に接続して被処理
水を移送等する場合に比して設備面での低コスト化が図
れるとともに、共通のブロワでエア供給しているので、
エア供給を効率よくしながら浄化槽を運転することが出
来、かつ、第1、第2、第3エア供給管に各別にエア供
給管を設ける場合に比しても、低コストな浄化槽を提供
することが出来る。
In other words, since the first, second and third air supply pipes are connected to one blower, the air supply pipe is connected to a pump or the like to transfer the water to be treated. As it can reduce costs and supply air with a common blower,
A septic tank can be operated while efficiently supplying air, and a low-cost septic tank is provided as compared with a case where air supply pipes are separately provided for the first, second, and third air supply pipes. I can do it.

【0008】さらに、前記ブロワから第3エア供給管
へ、エアを間欠的に供給可能にするためのエア供給量調
節手段を設けてあることから、第3エア供給管へのエア
供給を間欠的に行うことで、沈殿槽から消毒槽に移送す
るエアリフト管用のエア供給量を、浄化槽に流入する原
水の流量の変化に対し、沈殿槽から消毒槽に移送される
被処理水の移送量を大きく変化させないような量に設定
することが出来、このように設定することで、処理水の
平均放流量をトータルで安定した状態に制御することが
出来るようになった。もちろん、このような制御を行え
ば、剥離汚泥が処理水に混入して放出されることのない
エア供給量に設定する事が可能であることは言うまでも
ない。
Further, since an air supply amount adjusting means for intermittently supplying air from the blower to the third air supply pipe is provided, the air supply to the third air supply pipe is intermittently performed. By increasing the amount of air supplied to the air lift pipe transferred from the sedimentation tank to the disinfection tank, the transfer rate of the water to be treated transferred from the sedimentation tank to the The amount can be set so as not to change, and by setting in this way, the average discharge flow rate of the treated water can be controlled in a totally stable state. Needless to say, if such control is performed, it is possible to set the air supply amount such that the separated sludge is not mixed into the treated water and released.

【0009】[0009]

【発明の効果】したがって、処理水の平均放出量をトー
タルで安定した状態に制御することが出来るので、浄化
槽内での被処理水の生物処理を充分行うことができ、か
つ、剥離汚泥が処理水中に混入するおそれを少なくでき
るので、原水を高度に浄化した処理水として放流するこ
とができる高性能な浄化槽を、低コストで実現すること
が出来た。
As a result, the average discharge amount of the treated water can be controlled to a stable state in total, so that the biological treatment of the treated water in the septic tank can be sufficiently performed and the separated sludge is treated. Since the risk of being mixed into the water can be reduced, a high-performance septic tank capable of discharging raw water as highly purified treated water can be realized at low cost.

【0010】[0010]

【実施例】以下に本発明の実施例について図面に従って
説明する。図1に示すように、上流側から、嫌気瀘床槽
第1室N1及び嫌気瀘床槽第2室N2からなる嫌気瀘床
槽N、好気瀘床槽第1室E1及び好気瀘床槽第2室E2
からなる好気瀘床槽E、沈殿槽Pを、被処理水が自然移
流によりこの順に流れるように設け、また、沈殿槽Pの
上方には消毒槽Qを設けて浄化槽を構成してある。
Embodiments of the present invention will be described below with reference to the drawings. As shown in FIG. 1, from the upstream side, an anaerobic filter tank N comprising an anaerobic filter tank first chamber N1 and an anaerobic filter tank second chamber N2, an aerobic filter tank first chamber E1, and an aerobic filter bed. Tank second room E2
An aerobic filter tank E and a sedimentation tank P are provided so that water to be treated flows in this order by natural advection, and a disinfection tank Q is provided above the sedimentation tank P to constitute a purification tank.

【0011】前記嫌気瀘床槽第1室N1及び嫌気瀘床槽
第2室N2には、被処理水中の有機物を嫌気分解する嫌
気性微生物を生育して、その生物膜を定着させるために
瀘床F1,F2をそれぞれ設けてある。前記好気瀘床槽
第1室E1及び好気瀘床槽第2室E2には、被処理水中
の残りの有機物の分解やアンモニア性窒素の硝化反応等
を行う好気性微生物を定着させるための第1、第2接触
材C1,C2をそれぞれ別に設け、各室内に被処理水の
循環流を生ぜしめ、前記第1、第2接触材C1,C2に
定着させた好気性微生物に、有機物を含む被処理水をよ
く接触させ、且つこの好気性微生物に必要な酸素を与え
るエアーを供給するための散気管D1,D2を設けてあ
る。
The first anaerobic filter tank N1 and the second anaerobic filter tank N2 grow anaerobic microorganisms that anaerobically decompose organic substances in the water to be treated and filter them to fix their biofilms. Floors F1 and F2 are provided respectively. The first chamber E1 of the aerobic filter tank and the second chamber E2 of the aerobic filter tank are used to fix aerobic microorganisms that decompose the remaining organic matter in the water to be treated and perform a nitrification reaction of ammonia nitrogen. First and second contact materials C1 and C2 are separately provided, and a circulating flow of the water to be treated is generated in each chamber, and organic substances are removed from the aerobic microorganisms fixed on the first and second contact materials C1 and C2. Aeration tubes D1 and D2 are provided for bringing the treated water into good contact and supplying air for providing necessary oxygen to the aerobic microorganisms.

【0012】さらに接触材C1,C2に生物膜等が付着
しすぎて目詰まりを起こすことを防止するため、空気を
バブリングさせて、付きすぎた生物膜等を剥離汚泥とし
て剥離する逆洗管R1,R2が、接触材C1,C2の下
方に夫々設けられている。また、好気瀘床槽第1室E1
内の被処理水を嫌気瀘床槽第1室N1に返送するエアリ
フト管A1が、好気瀘床槽第1室E1内に、また、好気
瀘床槽第2室E2内の被処理水を嫌気瀘床槽第1室N1
に返送するエアリフト管A2が、好気瀘床槽第2室E2
内にそれぞれ立設してあると共に、浄化槽内上部で、嫌
気瀘床槽から好気瀘床槽にかけわたして設けてある横管
A3に、それぞれ接続することで返送管Aを構成してあ
る。
Further, in order to prevent clogging due to excessive adhesion of biofilms and the like to the contact materials C1 and C2, a backwash tube R1 for bubbling air to separate the excessively attached biofilms and the like as separation sludge. , R2 are provided below the contact members C1, C2, respectively. In addition, the first room E1 of the aerobic filter tank
An air lift pipe A1 for returning the water to be treated in the first chamber N1 to the anaerobic filter tank is provided in the first chamber E1 of the aerobic filter tank and the water to be treated in the second chamber E2 of the aerobic filter tank. The anaerobic filter tank 1st room N1
The air lift pipe A2 returned to the aerobic filter bed tank E2
In the upper part of the septic tank, return pipes A are formed by connecting to horizontal pipes A3 provided from the anaerobic filter tank to the aerobic filter tank, respectively.

【0013】次に、沈殿槽P及び消毒槽Qについて説明
すると、沈殿槽Pは下部において好気瀘床槽第2室E2
と連通させ、移流してきた剥離汚泥を沈殿除去する構成
にしてある。この沈殿槽Pと、消毒槽Qとの間には、U
字状のエアリフト管Uが設けてあり、このエアリフト管
Uを通じて被処理水を沈殿槽Pから消毒槽Qへ移送可能
に構成してある。
Next, the sedimentation tank P and the disinfection tank Q will be described.
To remove sediment sludge that has been transferred. Between the sedimentation tank P and the disinfection tank Q, U
A letter-shaped air lift pipe U is provided, and the water to be treated can be transferred from the sedimentation tank P to the disinfection tank Q through the air lift pipe U.

【0014】尚、エアリフト管UはU字状であるが故
に、沈殿槽P上部の、剥離汚泥の浮遊量の少ない被処理
液のみを消毒槽Qに移動することが出来るようになって
おり、また、浄化槽内の被処理水量が減少した場合に
は、被処理水の移送を停止し、浄化槽内の被処理水量を
ある程度の量に維持できるようになっている。
Since the air lift pipe U has a U-shape, only the liquid to be treated in the upper part of the sedimentation tank P having a small amount of suspended sludge can be moved to the disinfection tank Q. When the amount of water to be treated in the septic tank decreases, the transfer of the water to be treated is stopped, and the amount of water to be treated in the septic tank can be maintained at a certain level.

【0015】前記散気管D1,D2は、第1エア供給管
1を介してブロワBに接続してあり、前記エアリフト管
A1,A2は、第2エア供給管2を介して前記ブロワB
に接続してあり、また、エアリフト管Uは第3エア供給
管3を介して前記ブロワBに接続してあり、さらに、逆
洗管R1,R2は第4エア供給管4を介して前記ブロワ
Bに接続してあり、さらに、1つのブロワBからのエア
供給で、それぞれ機能するようになっている。
The air diffusers D1, D2 are connected to a blower B via a first air supply pipe 1, and the air lift pipes A1, A2 are connected to the blower B via a second air supply pipe 2.
The air lift pipe U is connected to the blower B via a third air supply pipe 3, and the backwash pipes R1 and R2 are connected to the blower via a fourth air supply pipe 4. B, and each of them functions by supplying air from one blower B.

【0016】また、第3エア供給管3とブロワBとの間
にはさらにエア供給量調節手段Mを設けてあり、沈殿槽
Pから消毒槽Qに被処理水を間欠的に移送し、トータル
で浄化槽から外に放流される処理水の流量を既定量に調
整出来るようにしてあり、かつ、第4エア供給管4とブ
ロワBとの間には、さらにエア流路開閉機構Vを設けて
あり、定期的に(1日1回15分程度)接触材を逆洗す
ることが出来るようにしてある。
An air supply adjusting means M is further provided between the third air supply pipe 3 and the blower B to intermittently transfer the water to be treated from the sedimentation tank P to the disinfection tank Q. The flow rate of the treated water discharged from the septic tank can be adjusted to a predetermined amount, and an air flow opening / closing mechanism V is further provided between the fourth air supply pipe 4 and the blower B. Yes, the contact material can be backwashed periodically (about 15 minutes once a day).

【0017】この浄化槽1においては、沈殿槽P、消毒
槽Qをのぞく、各槽、N1,N2,E1,E2間に渡る
被処理水の移動は、自然移流方式でおこなわれる。そし
て、エアリフト管A1,A2へのエア供給により、返送
管Aが作動されて被処理水の返送がおこなわれるととも
に、沈殿槽Pと消毒槽Qとの間においては、エアリフト
管Uへの間欠的なエア供給により、長期的にみて定常的
に被処理水の移送が行われる。
In this purification tank 1, the water to be treated moves between each tank and N1, N2, E1, and E2, except for the settling tank P and the disinfection tank Q, by a natural advection method. Then, by the supply of air to the air lift pipes A1 and A2, the return pipe A is operated to return the water to be treated, and intermittently to the air lift pipe U between the sedimentation tank P and the disinfection tank Q. By the appropriate air supply, the water to be treated is constantly transferred over a long period of time.

【0018】即ち、好気瀘床槽第2室E2の被処理水
は、エアリフト管A1により嫌気瀘床槽第1室N1に返
送される。このとき、この被処理水には、好気瀘床槽第
2室E2内に配設される接触材C2から剥離した剥離汚
泥と、アンモニア分解を完了した硝化液が含まれる。こ
れにより、硝化液は嫌気濾床槽第1室及び嫌気瀘床槽第
2室において良好に脱窒作用を受け、被処理水は浄水さ
れる。さらにここで、各槽、N1,N2,E1,E2間
においては前述のように被処理水の移動が起こる。この
結果、嫌気瀘床槽第1、第2室N1,N2で分解処理、
脱窒処理が進行する。即ち、浄化槽1内に於ける被処理
水の循環に伴って、剥離汚泥の移動供給が起こるととも
に、好気濾床槽E1,E2内の硝化液もその脱窒処理に
適する嫌気瀘床槽N1,N2内へ移動し、処理が促進さ
れるのである。従って、剥離汚泥を返送出来るから、浄
化槽1内の処理を充分に進められると共に好気瀘床槽第
2室E2内の剥離汚泥の濃度も低く抑えられる。
That is, the water to be treated in the second chamber E2 of the aerobic filter tank is returned to the first chamber N1 of the anaerobic filter tank by the air lift pipe A1. At this time, the water to be treated includes the separated sludge separated from the contact material C2 disposed in the second chamber E2 of the aerobic filter bed, and the nitrification liquid that has been completely decomposed with ammonia. As a result, the nitrification liquid is satisfactorily denitrified in the first chamber of the anaerobic filter tank and the second chamber of the anaerobic filter tank, and the water to be treated is purified. Further, here, the water to be treated moves between the tanks N1, N2, E1, and E2 as described above. As a result, decomposition treatment is performed in the first and second chambers N1 and N2 of the anaerobic filter tank.
The denitrification process proceeds. That is, with the circulation of the water to be treated in the septic tank 1, the movement and supply of the separated sludge occur, and the nitrifying liquid in the aerobic filter tanks E1 and E2 also converts the anaerobic filter tank N1 suitable for the denitrification treatment. , N2 to accelerate the processing. Therefore, since the separated sludge can be returned, the treatment in the septic tank 1 can be sufficiently advanced, and the concentration of the separated sludge in the second chamber E2 of the aerobic filter tank can be suppressed to a low level.

【0019】さらに、被処理水は好気濾床槽第2室E2
の下部から沈殿槽Pに導かれ、前記エアリフト管Uによ
って消毒槽Qに導かれる。このとき、エアリフト移送水
量を例えば対象人員が5〜10人程度のし尿処理用浄化
槽では4リットル/分程度としておき、運転、停止を交
互に行う間欠運転を行えば、剥離汚泥の浄化槽外への流
出を防止できるとともに、原水の流入量の変動に伴う処
理水の放流量を既定量に設定し、長期的にみて変動を抑
制できた。従って浄化槽内では硝化、脱窒作用が充分発
揮されることになる。
Further, the water to be treated is aerobic filter bed tank second chamber E2.
From the lower part to the settling tank P, and to the disinfection tank Q by the air lift pipe U. At this time, the amount of water transferred by the air lift is set to, for example, about 4 liters / minute in a septic tank for human waste treatment with about 5 to 10 target personnel, and if an intermittent operation of alternately operating and stopping is performed, the separated sludge is discharged to the outside of the septic tank. In addition to preventing outflow, the discharge rate of treated water was set to a predetermined amount due to fluctuations in the inflow of raw water, and fluctuations could be suppressed over the long term. Therefore, the nitrification and denitrification effects are sufficiently exhibited in the septic tank.

【0020】消毒槽Qに導かれた被処理水は、固形消毒
剤と接触して消毒された後、放流口Zから外部に処理水
として放流されるように各槽を形成してある。
Each of the tanks is formed such that the water to be treated introduced into the disinfecting tank Q is disinfected by contact with a solid disinfectant and then discharged from the discharge port Z to the outside as treated water.

【0021】従って、前記流入口Iから入って来た原水
は、上述のような処理を経た後放流されるので、高度に
浄化された処理水として排水できることになる。
Accordingly, the raw water entering from the inlet I is discharged after the above-mentioned treatment, so that it can be discharged as highly purified treated water.

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

【図1】本発明の実施例における浄化槽の縦断側面図FIG. 1 is a vertical side view of a septic tank according to an embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 第1エア供給管 2 第2エア供給管 3 第3エア供給管 B ブロワ E 好気濾床槽 M エア供給量調節手段 N 嫌気濾床槽 P 沈殿槽 Q 消毒槽 DESCRIPTION OF SYMBOLS 1 1st air supply pipe 2 2nd air supply pipe 3 3rd air supply pipe B Blower E Aerobic filter bed tank M Air supply control means N Anaerobic filter bed tank P Precipitation tank Q Disinfection tank

───────────────────────────────────────────────────── フロントページの続き (72)発明者 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 (72)発明者 浜田 勝己 滋賀県甲賀郡甲西町高松2番地の1 株 式会社クボタ 滋賀工場内 (56)参考文献 特開 平5−4030(JP,A) 特開 平4−200792(JP,A) 特開 平5−50081(JP,A) 特開 平5−138184(JP,A) (58)調査した分野(Int.Cl.6,DB名) C02F 3/00──────────────────────────────────────────────────続 き Continuing from the front page (72) Inventor Kazuyuki Honda 1 at 2, Takamatsu, Kosai-cho, Koga-gun, Koka-gun, Shiga Prefecture Inside the Kubota Shiga Plant (72) Katsumi Hamada 2, Takamatsu, Kosai-cho, Koga-gun, Shiga 1 Kubota Corporation Shiga Factory (56) References JP-A-5-4030 (JP, A) JP-A-4-200792 (JP, A) JP-A-5-5081 (JP, A) JP-A-5 −138184 (JP, A) (58) Fields investigated (Int. Cl. 6 , DB name) C02F 3/00

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 上流側から嫌気濾床槽(N)、好気濾床
槽(E)、沈殿槽(P)を被処理水が自然移流によりこ
の順に流れるように設けるとともに、消毒槽(Q)を設
け、前記好気濾床槽(E)への散気用の第1エア供給管
(1)と、下流側から上流側へ被処理水を返送する返送
管用の第2エア供給管(2)と、被処理水を前記沈殿槽
から前記消毒槽に移送するエアリフト管用の第3エア供
給管(3)とを連設してあり、各エア供給管(1),
(2),(3)はブロワ(B)に接続してある浄化槽であ
って、 前記第1、第2、第3エア供給管(1),(2),(3)を
一つのブロワ(B)に接続するとともに、前記ブロワ
(B)から第3エア供給管(3)へ、エアを間欠的に供
給可能にするためのエア供給量調節手段(M)を設けた
浄化槽。
An anaerobic filter tank (N), an aerobic filter tank (E), and a sedimentation tank (P) are provided from the upstream side so that water to be treated flows in this order by natural advection, and a disinfection tank (Q) is provided. ), And a first air supply pipe (1) for diffusing air into the aerobic filter bed tank (E) and a second air supply pipe (for returning water to be treated from the downstream side to the upstream side). 2) and a third air supply pipe (3) for an air lift pipe for transferring the water to be treated from the sedimentation tank to the disinfection tank, and each of the air supply pipes (1),
(2) and (3) are septic tanks connected to the blower (B), and the first, second and third air supply pipes (1), (2) and (3) are connected to one blower ( B) and a purification tank provided with an air supply amount adjusting means (M) for intermittently supplying air from the blower (B) to the third air supply pipe (3).
JP22678593A 1993-09-13 1993-09-13 Septic tank Expired - Fee Related JP2839065B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22678593A JP2839065B2 (en) 1993-09-13 1993-09-13 Septic tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22678593A JP2839065B2 (en) 1993-09-13 1993-09-13 Septic tank

Publications (2)

Publication Number Publication Date
JPH0780484A JPH0780484A (en) 1995-03-28
JP2839065B2 true JP2839065B2 (en) 1998-12-16

Family

ID=16850581

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22678593A Expired - Fee Related JP2839065B2 (en) 1993-09-13 1993-09-13 Septic tank

Country Status (1)

Country Link
JP (1) JP2839065B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100459331B1 (en) * 2002-12-09 2004-12-03 대명엔텍(주) Sweage disposal equipment being highly processing type with aspirated diffusers for recirculating sludge using by air stone
JP2008246329A (en) * 2007-03-29 2008-10-16 Kubota Corp Septic tank
JP5341377B2 (en) * 2008-03-17 2013-11-13 株式会社クボタ Septic tank

Also Published As

Publication number Publication date
JPH0780484A (en) 1995-03-28

Similar Documents

Publication Publication Date Title
RU2135420C1 (en) Waste water treatment method and installation
US7311833B2 (en) Zero excess sludge membrane bioreactor
KR20060090417A (en) System and method for advanced treatment of nitrogen and phosphorus using microorganism and separation membrane
US20130264282A1 (en) Process, apparatus and membrane bioreactor for wastewater treatment
KR101190472B1 (en) A none piping membrane bioreactor with circulation-agitater
KR100279843B1 (en) Wastewater Contact Aeration Purification System and Contact Aeration Purification Method
JP2839065B2 (en) Septic tank
Su et al. Treatment of piggery wastewater by contact aeration treatment in coordination with the anaerobic fermentation of three‐step piggery wastewater treatment (TPWT) process in Taiwan
KR20060085770A (en) System and method for advanced sewage treatment using microorganism and separation membrane
KR100869304B1 (en) High effective treatment apparatus of sewage and wastewater
KR20030097075A (en) Hybrid Submerged Plate Type Membrane Bioreactor Using microfilter Combined With Biofilm-Activated Carbon for Advanced Treatment of Sewage and Wastewater
KR19990083645A (en) Organic material and nitrogen, phosphate removal method using intermitted aeration process and plate type microfiltration membrane
KR102052163B1 (en) Wastewater treatment apparatus and method
KR100473710B1 (en) Apparatus and method for disposing sewage with high accuracy
KR100304068B1 (en) Biological Water Treatment Apparatus Using Biological Membrane Filtration and Process thereof(SBF)
KR200381627Y1 (en) System for advanced sewage treatment using microorganism and separation membrane
KR100795072B1 (en) Treatment method and apparatus for wastewater include excrementitious matter of domestic animal
CN219621038U (en) Sewage treatment plant of MABR membrane purification spring water
CN213388243U (en) Industrial wastewater treatment device
JP2673488B2 (en) Method and apparatus for treating organic wastewater
KR200307954Y1 (en) Apparatus for disposing sewage with high accuracy
CN111499106B (en) Integrated sewage treatment device and method
JPH0516000Y2 (en)
JP3115967B2 (en) Operation method of septic tank and septic tank
KR200385109Y1 (en) System for advanced treatment of nitrogen and phosphorus using microorganism and separation membrane

Legal Events

Date Code Title Description
LAPS Cancellation because of no payment of annual fees