JPH0537397U - Septic tank - Google Patents
Septic tankInfo
- Publication number
- JPH0537397U JPH0537397U JP8551891U JP8551891U JPH0537397U JP H0537397 U JPH0537397 U JP H0537397U JP 8551891 U JP8551891 U JP 8551891U JP 8551891 U JP8551891 U JP 8551891U JP H0537397 U JPH0537397 U JP H0537397U
- Authority
- JP
- Japan
- Prior art keywords
- tank
- filter bed
- treated water
- anaerobic filter
- flow rate
- 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
Landscapes
- Treatment Of Biological Wastes In General (AREA)
Abstract
(57)【要約】
【構成】 汚水流入側から嫌気濾床槽Nと接触ばっ気槽
Eをこの順に装備し、接触ばっ気槽Eから嫌気濾床槽N
に処理水を返送する返送路Bを設け、返送路の途中に堰
板Wを取り付け、返送処理水を通過させる流量制限用孔
Hを堰板Wに形成してある。
【効果】 簡単な改良でありながら、返送路内の水位の
変化に伴う流量の変動を従来よりも小さくして、返送処
理水の流量管理を容易にし、安定した水処理のできる浄
化槽を提供することができた。
(57) [Summary] [Structure] An anaerobic filter bed tank N and a contact aeration tank E are installed in this order from the sewage inflow side, and the contact aeration tank E to the anaerobic filter bed tank N are installed.
A return path B for returning the treated water is provided in the back wall, a dam plate W is attached in the middle of the return path, and a flow rate limiting hole H for passing the returned treated water is formed in the dam plate W. [Effect] Although it is a simple improvement, the fluctuation of the flow rate due to the change of the water level in the return passage is made smaller than before, the flow rate of the return treated water is easily controlled, and a septic tank capable of stable water treatment is provided. I was able to.
Description
【0001】[0001]
本考案は、汚水流入側から嫌気濾床槽と接触ばっ気槽をこの順に装備し、前記 接触ばっ気槽から前記嫌気濾床槽に処理水を返送する返送路を設けてある浄化槽 に関する。 The present invention relates to a septic tank equipped with an anaerobic filter bed tank and a contact aeration tank in this order from the sewage inflow side, and a return passage for returning treated water from the contact aeration tank to the anaerobic filter bed tank.
【0002】[0002]
従来、この種の浄化槽にあって、前記接触ばっ気槽から前記嫌気濾床槽に返送 する処理水の水位の変化に伴う流量の変動を緩和するために前記返送路の途中に 、Vノッチを有する堰板を設けることが考えられていた。 Conventionally, in this type of septic tank, a V-notch is provided in the middle of the return passage in order to mitigate the fluctuation of the flow rate due to the change in the water level of the treated water returned from the contact aeration tank to the anaerobic filter bed tank. It was considered to provide the weir board which has.
【0003】[0003]
ところが、この従来の構成では、前記変動をある程度緩和できるものの、変動 が充分小さくなるとはいい難く、そのため、まだ安定した水処理が行いにくい欠 点があった。例えば、過剰循環水量に設定された場合、嫌気濾床槽内の好気化に よる脱窒能の低下や、ピーク流入時に、循環水量が加算された移流水量により、 貯留懸濁物が次槽へ移流しやすい等の問題があった。 そこで、本考案の目的は、返送路内の水位の変化に伴う流量の変動を更に小さ くして、返送処理水の流量管理を容易にし、安定した水処理のできる浄化槽を提 供することにある。 However, with this conventional configuration, although it is possible to alleviate the fluctuation to some extent, it is difficult to say that the fluctuation is sufficiently small, and therefore there is a drawback that stable water treatment is still difficult to perform. For example, when the amount of excess circulating water is set, the retained debris is transferred to the next tank due to the decrease in denitrification capacity due to aerobicization in the anaerobic filter bed tank, and the advected water volume to which the circulating water volume is added at the time of peak inflow. There were problems such as easy migration. Therefore, an object of the present invention is to provide a septic tank capable of performing stable water treatment by further reducing the fluctuation of the flow rate due to the change of the water level in the return passage, facilitating the flow rate control of the return treated water.
【0004】[0004]
この目的を達成するための本考案による浄化槽の特徴構成は、接触ばっ気槽か ら嫌気濾床槽に処理水を返送する返送路の途中に堰板を取り付け、前記嫌気濾床 槽への返送処理水を通過させる流量制限用孔を前記堰板に形成してあることにあ り、その作用効果は次の通りである。 To achieve this purpose, the septic tank according to the present invention is characterized in that a weir plate is attached in the middle of the return path for returning the treated water from the contact aeration tank to the anaerobic filter tank, and it is returned to the anaerobic filter tank. Since the flow restricting hole for passing the treated water is formed in the dam plate, the function and effect thereof are as follows.
【0005】[0005]
【作用】 堰板に流量制限用孔を形成した本考案の構成にしてあると、水位が流量制限用 孔から上にありさえすれば、どの高さにあったとしても堰板を通過する処理水の 流束断面積は流量制限用孔の断面積そのものであるから一定である。従って、堰 板にVノッチを形成してあるために水位が上昇すれば上昇するほど、Vノッチ下 端までの水深の2乗に比例して前記流束の断面積が増加する従来の構成における 場合よりも、水位の変化に伴う流量の変化を小さく抑えることができる。 ちなみに、堰板にVノッチを形成した構成における場合、流量はVノッチの下 端までの水深の2.5乗に比例して大きく変動するのに比し、堰板に流量制限用 孔を形成した本考案による場合は流量制限用孔までの水深の0.5乗に比例する 小さな流量変動に抑えることができる。[Operation] With the structure of the present invention in which the flow restricting hole is formed in the weir plate, as long as the water level is above the flow restricting hole, the process of passing through the weir plate at any height The flux cross-sectional area of water is constant because it is the cross-sectional area of the flow restriction hole itself. Therefore, in the conventional configuration, the cross section area of the flux increases in proportion to the square of the water depth up to the lower end of the V notch as the water level rises because the V notch is formed in the dam plate. As compared with the case, the change in the flow rate due to the change in the water level can be suppressed to be smaller. By the way, in the case of the structure in which the V notch is formed on the weir plate, the flow rate changes greatly in proportion to the 2.5th power of the water depth to the lower end of the V notch, whereas the flow restricting hole is formed on the weir plate. According to the present invention, it is possible to suppress a small flow rate fluctuation proportional to the 0.5th power of the water depth up to the flow rate limiting hole.
【0006】[0006]
特に新たな装置を設けることなく、堰板に流量制限用孔を形成するだけの簡単 な改良でありながら、返送路内の水位の変化に伴う流量の変動を従来よりも更に 小さくして、返送処理水の流量管理を容易にし、循環式嫌気・好気濾床法による 安定した水処理のできる浄化槽を提供することができた。 It is a simple improvement that only a flow restriction hole is formed in the weir plate without installing a new device, but the fluctuation of the flow rate due to the change of the water level in the return passage is made smaller than before and the return is performed. We were able to provide a septic tank that facilitates the management of the flow rate of treated water and enables stable water treatment by the circulating anaerobic / aerobic filter bed method.
【0007】[0007]
以下、本願の実施例の構成を図面に基づいて説明する。 この浄化槽1は、図1に示すように、上流側から、嫌気濾床槽第1室N1と嫌 気濾床槽第2室N2から成る嫌気濾床槽N、接触ばっ気槽E、そして沈殿槽Pを 、この順に備えて構成されている。 以下、各槽N、E、Pについてさらに詳細に説明する。 嫌気濾床槽第1室N1は、流入口2から流入する処理水中の粗大浮遊物を除去 するとともに、嫌気濾床槽第2室N2と同様に嫌気分解処理を行う。そのため、 この嫌気濾床槽第1室N1と嫌気濾床槽第2室N2には、処理水中の有機物を嫌 気分解する嫌気性微生物を生息させ、その生物膜をとして定着させるために、第 1、第2濾床F1、F2が設けられている。ここで、嫌気濾床槽第1室N1の第 1濾床F1は、目詰まりしにくい粗い格子間隔のハニカムチューブ状濾材メッシ ュで形成され、嫌気濾床槽第2室N2の第2濾床F2は嫌気濾床槽第1室N1の 第1濾床F1よりも密に構成されてる。嫌気濾床槽Nの上方にはマンホールM’ を設けてある。 次に前記接触ばっ気槽Eについて説明する。接触ばっ気槽Eは、処理水中の有 機物やアンモニア性窒素等を酸化分解するものであり、この目的で好気性微生物 を定着させる接触材Cが備えられている。さらに、接触ばっ気槽E内に処理水の 循環流を生ぜしめて、有機物を含む処理水を、接触材Cに定着させた好気性微生 物とよく接触させるとともに、この好気性微生物に必要な酸素を与えるためのエ アーを供給する散気管Dが接触ばっ気槽E内に配設されている。接触ばっ気槽E の上方にはマンホールMを設けてある。 次に、前記沈殿槽Pについて説明する。この沈殿槽Pには消毒槽Qを設け、接 触ばっ気槽Eからの排水に対して、その浮遊懸濁物を沈殿除去した後、消毒して 放流口4から放流するようにしてある。 Hereinafter, the configuration of the embodiment of the present application will be described with reference to the drawings. As shown in FIG. 1, this septic tank 1 includes an anaerobic filter bed tank N composed of an anaerobic filter bed tank first chamber N1 and an anaerobic filter bed tank second chamber N2, a contact aeration tank E, and a sedimentation apparatus from the upstream side. The tank P is provided in this order. Hereinafter, each tank N, E, P will be described in more detail. The anaerobic filter bed tank first chamber N1 removes coarse suspended matter in the treated water flowing from the inflow port 2, and performs anaerobic decomposition treatment in the same manner as the anaerobic filter bed tank second chamber N2. Therefore, in the anaerobic filter bed first chamber N1 and the anaerobic filter bed second chamber N2, anaerobic microorganisms that anaerobically decompose organic substances in the treated water are made to live, and the biofilm thereof is fixed as First and second filter beds F1 and F2 are provided. Here, the first filter bed F1 of the first chamber N1 of the anaerobic filter bed is formed by a honeycomb tubular filter medium mesh with a coarse lattice spacing that is unlikely to be clogged, and the second filter bed of the second chamber N2 of the anaerobic filter bed tank is used. F2 is constructed more densely than the first filter bed F1 in the first chamber N1 of the anaerobic filter bed. A manhole M'is provided above the anaerobic filter bed tank N. Next, the contact aeration tank E will be described. The contact aeration tank E is for oxidatively decomposing organic substances, ammonia nitrogen and the like in the treated water, and is provided with a contact material C for fixing aerobic microorganisms for this purpose. Further, a circulating flow of the treated water is generated in the contact aeration tank E so that the treated water containing organic matter is brought into good contact with the aerobic microorganisms fixed on the contact material C, and this aerobic microorganism is required. An air diffuser D for supplying air for giving oxygen is arranged in the contact aeration tank E. A manhole M is provided above the contact aeration tank E 1. Next, the settling tank P will be described. The settling tank P is provided with a disinfecting tank Q, and the wastewater from the contact aeration tank E is subjected to sedimentation and removal of its suspended suspension, and then disinfected and discharged from the discharge port 4.
【0008】 以下に、本願による浄化槽1の返送路たる移送管Bに関して説明をする。 この浄化槽1は、図1に示すように、接触ばっ気槽Eから嫌気濾床槽第1室N 1に硝化液を含む処理水を返送する移送管Bを設け、この移送管Bに接触ばっ気 槽Eの処理水を揚水するエアーリフトポンプAを設けてある。 エアーリフトポンプAは下部に処理水の吸引口とエアーリフト用エアーの受け 入れ口を設けた中空のパイプを垂直に配しただけの簡単な構造を有するもので、 その上端は、図4及び図5に縦断側面図と横断正面図で示すように、T字管T’ を接続して前後に分岐し、一方の分岐管を前記移送管Bに向けて接続すると共に 、その接続部の管内の予想水面あたりの高さに、処理水の表面の波立ちを抑える ための波動防止バッフル3(邪魔板)を設けてある。もう一方の分岐管は、その 端部に、水面を適切な高さに保ち、余剰の揚水が接触ばっ気槽Eに戻るように水 位設定用堰板5を設けて開口部6を形成してある。 移送管Bの途中には、図1〜図3に示すように、空気抜き口7を上に向けた状 態でT字管Tを介在させてある。T字管T内には、前記空気抜き口7から見やす い中央付近に、返送処理水の流れの方向に直角に堰板Wを取り付けてある。この 堰板Wには、返送処理水をその流量を制限しながら通過させる円形の流量制限用 孔Hを図3に示すように、垂直中心線上に形成すると共に、所定の流量に対応す る水位のところに、この水位を確認するための水位設定用指示線Sを設けてある 。 尚、このT字管Tは、前記マンホールM’を開けると、浄化槽の外から見やす い位置に設けてある。 以上の構成により、接触ばっ気槽Eから嫌気濾床槽第1室N1への返送処理水 の流量の管理が容易な浄化槽を得ることができた。The transfer pipe B, which is the return path of the septic tank 1 according to the present application, will be described below. As shown in FIG. 1, the septic tank 1 is provided with a transfer pipe B for returning the treated water containing the nitrifying solution from the contact aeration tank E to the first chamber N 1 of the anaerobic filter bed, and the contact pipe B is contacted with the transfer pipe B. An air lift pump A for pumping the treated water in the air tank E is provided. The air lift pump A has a simple structure in which a hollow pipe having a suction port for treated water and a receiving port for air for air lift is arranged vertically in the lower part. As shown in a vertical side view and a cross-sectional front view in FIG. 5, a T-shaped tube T ′ is connected to branch in the front and back, and one branch tube is connected toward the transfer tube B, and at the same time, the inside of the connecting tube is connected. A wave-prevention baffle 3 (baffle plate) is provided at the expected height of the surface of the water to suppress ripples on the surface of the treated water. The other branch pipe has a water level setting dam plate 5 at its end so that the water surface is kept at an appropriate height and excess pumped water returns to the contact aeration tank E, and an opening 6 is formed. There is. As shown in FIGS. 1 to 3, a T-shaped tube T is interposed in the middle of the transfer tube B with the air vent port 7 facing upward. In the T-shaped tube T, a weir plate W is installed in the vicinity of the center where it is easy to see from the air vent 7 at right angles to the direction of the flow of the treated return water. As shown in FIG. 3, a circular flow restricting hole H is formed in the dam W to allow the returned treated water to pass therethrough while restricting the flow rate thereof, and the water level corresponding to a predetermined flow rate is formed on the vertical center line. However, a water level setting indicator line S for confirming the water level is provided. The T-shaped tube T is provided at a position where it can be easily seen from the outside of the septic tank when the manhole M'is opened. With the above configuration, it was possible to obtain a septic tank in which the flow rate of the return-treated water from the contact aeration tank E to the anaerobic filter bed first chamber N1 can be easily controlled.
【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。It should be noted that reference numerals are added to the claims of the utility model for convenience of comparison with the drawings, but the invention is not limited to the configuration of the accompanying drawings by the entry.
【図1】本願の実施例における浄化槽の縦断側面図FIG. 1 is a vertical sectional side view of a septic tank according to an embodiment of the present application.
【図2】堰板付近縦断側面図[Fig. 2] Side view of a vertical section near the weir plate
【図3】堰板付近横断正面図[Fig. 3] Front view crossing the barrier plate
【図4】波動防止バッフル付近縦断側面図[Fig. 4] Side view of the vertical section near the wave prevention baffle
【図5】波動防止バッフル付近横断正面図[Fig. 5] Front view of the vicinity of a wave prevention baffle
N 嫌気濾床槽 E 接触ばっ気槽 B 返送路 W 堰板 H 流量制限用孔 N Anaerobic filter bed E Contact aeration tank B Return path W Weir plate H Flow restriction hole
───────────────────────────────────────────────────── 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 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Dai Harada, 2 Takamatsu, Kosai-cho, Koga-gun, Shiga Prefecture, 1st in Kubota Shiga Plant, Inc. (72) Kazuyuki Honda, 1 2 Takamatsu, Kosai-cho, Koga-gun, Shiga Prefecture Kubota Shiga Factory Co., Ltd.
Claims (1)
ばっ気槽(E)をこの順に装備し、前記接触ばっ気槽
(E)から前記嫌気濾床槽(N)に処理水を返送する返
送路(B)を設けてある浄化槽であって、 前記返送路の途中に堰板(W)を取り付け、前記嫌気濾
床槽(N)への返送処理水を通過させる流量制限用孔
(H)を前記堰板(W)に形成してある浄化槽。1. A anaerobic filter bed tank (N) and a contact aeration tank (E) are installed in this order from the sewage inflow side, and the treated water is transferred from the contact aeration tank (E) to the anaerobic filter bed tank (N). A septic tank provided with a return passage (B) for returning the water, wherein a weir plate (W) is attached in the middle of the return passage to limit the flow rate of the return-treated water to the anaerobic filter bed tank (N). A septic tank having holes (H) formed in the barrier plate (W).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1991085518U JP2565652Y2 (en) | 1991-10-21 | 1991-10-21 | Septic tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1991085518U JP2565652Y2 (en) | 1991-10-21 | 1991-10-21 | Septic tank |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0537397U true JPH0537397U (en) | 1993-05-21 |
| JP2565652Y2 JP2565652Y2 (en) | 1998-03-18 |
Family
ID=13861132
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1991085518U Expired - Lifetime JP2565652Y2 (en) | 1991-10-21 | 1991-10-21 | Septic tank |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2565652Y2 (en) |
Cited By (2)
| 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 |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0222072U (en) * | 1988-07-28 | 1990-02-14 | ||
| JPH02222791A (en) * | 1989-02-25 | 1990-09-05 | Toto Ltd | Septic tank which can adjust reflux rate from aerobic treatment chamber to anaerobic treatment chamber |
| JPH0326395A (en) * | 1989-06-23 | 1991-02-04 | Toto Ltd | Septic tank capable of adjusting reflux amount from aerobic treating chamber to anaerobic treating chamber |
-
1991
- 1991-10-21 JP JP1991085518U patent/JP2565652Y2/en not_active Expired - Lifetime
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0222072U (en) * | 1988-07-28 | 1990-02-14 | ||
| JPH02222791A (en) * | 1989-02-25 | 1990-09-05 | Toto Ltd | Septic tank which can adjust reflux rate from aerobic treatment chamber to anaerobic treatment chamber |
| JPH0326395A (en) * | 1989-06-23 | 1991-02-04 | Toto Ltd | Septic tank capable of adjusting reflux amount from aerobic treating chamber to anaerobic treating chamber |
Cited By (2)
| 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 |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2565652Y2 (en) | 1998-03-18 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| EXPY | Cancellation because of completion of term |