JPH0720589B2 - Clear water discharge control device in wastewater treatment - Google Patents

Clear water discharge control device in wastewater treatment

Info

Publication number
JPH0720589B2
JPH0720589B2 JP63175358A JP17535888A JPH0720589B2 JP H0720589 B2 JPH0720589 B2 JP H0720589B2 JP 63175358 A JP63175358 A JP 63175358A JP 17535888 A JP17535888 A JP 17535888A JP H0720589 B2 JPH0720589 B2 JP H0720589B2
Authority
JP
Japan
Prior art keywords
water
pipe
exhaust
control device
trough
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 - Lifetime
Application number
JP63175358A
Other languages
Japanese (ja)
Other versions
JPH0226693A (en
Inventor
一 伊藤
輝久 吉田
Original Assignee
日立機電工業株式会社
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 日立機電工業株式会社 filed Critical 日立機電工業株式会社
Priority to JP63175358A priority Critical patent/JPH0720589B2/en
Publication of JPH0226693A publication Critical patent/JPH0226693A/en
Publication of JPH0720589B2 publication Critical patent/JPH0720589B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

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  • Activated Sludge Processes (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は下水、その他の廃水を回分式活性汚泥法にて処
理する装置において、その処理後の上澄水をサイホン現
象を利用して確実に排出する装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial field of application] The present invention relates to a device for treating sewage and other wastewater by the batch activated sludge method, and ensures that the treated supernatant water is treated by utilizing the siphon phenomenon. The present invention relates to a discharging device.

〔従来の技術〕[Conventional technology]

下水・工場廃水・その他の廃水を処理する方法として回
分式活性汚泥法がある。これは一つの処理槽内に供給さ
れる廃水、すなわち原水を一定量流入せしめ、これを曝
気して微生物による活性処理を行なった後、原水中に浮
遊する固形物(主として汚泥)を沈澱させ、次いで上澄
水(処理水)と沈澱汚泥とを分離して個別的に排出し、
この原水流入→曝気→沈澱→放流(排水)の工程を繰り
返し行なうものである。そして常に変動する水位に対し
て追従するようにして上澄水を排出する装置としては実
開昭60−104204号公報、実開昭59−7092号公報等に開示
されたものが知られている。
The batch activated sludge method is a method for treating sewage, industrial wastewater, and other wastewater. This is a wastewater supplied into one treatment tank, that is, a certain amount of raw water is made to flow in, and after aerating this to perform active treatment with microorganisms, solid matters (mainly sludge) floating in the raw water are precipitated, Next, supernatant water (treated water) and sedimented sludge are separated and discharged individually,
This process of inflowing raw water → aeration → precipitation → discharge (drainage) is repeated. As devices for discharging the supernatant water so as to follow the constantly changing water level, those disclosed in Japanese Utility Model Publication No. 60-104204 and Japanese Utility Model Publication No. 59-7092 are known.

前者は、フロートに設けた昇降装置にて排水管の吸引口
を昇降し、フロートと吸引口間を開閉させて上澄水を流
入させるものであり、後者は排水パイプに取り付けたフ
ロートタンクにエアを吸入・排水して、排水パイプ全体
を水面上下に昇降させるものである。
The former is to raise and lower the suction port of the drain pipe with the lifting device installed on the float, and to open and close the space between the float and the suction port to allow the clear water to flow in, and the latter is to feed air to the float tank attached to the drain pipe. It inhales and drains, and raises and lowers the entire drainage pipe above and below the water surface.

〔発明が解決しようとする課題〕[Problems to be Solved by the Invention]

前者は、吸引口とフロート間のシール部分から汚水・ス
カムが流入する恐れがあり、後者は排水パイプ全体をフ
ロートタンクの空気吸入排出でフロート全体を昇降する
ため、装置として大がかりとなってしまう欠点があっ
た。
The former may cause sewage and scum to flow in from the seal between the suction port and the float, while the latter raises and lowers the entire float by sucking air in and out of the float tank over the entire drain pipe. was there.

本発明は、簡易な方法で上澄水をサイホン現象利用にて
確実に排水することを可能にする排水処理における上澄
水排出制御装置を提供することを目的とする。
It is an object of the present invention to provide a supernatant water discharge control device in wastewater treatment that enables reliable drainage of supernatant water using a siphon phenomenon by a simple method.

〔課題を解決するための手段〕[Means for Solving the Problems]

集水トラフに上澄水排出時サイホンを形成するための排
気配管系とサイホンブレーク配管系とを接続し、かつこ
の各配管系の機器を制御装置にて制御する。そして、前
記排気配管系には集水トラフと排気ユニット間を排気用
ホースで接続し、かつ排気ユニットの排気用電磁弁・真
空ポンプを集水トラフ内の負圧を検出する圧力スイッチ
に接続した制御装置にて制御する。
An exhaust pipe system for forming a siphon at the time of discharging clear water and a siphon break pipe system are connected to a water collection trough, and the equipment of each pipe system is controlled by a controller. Then, in the exhaust piping system, a water collecting trough and an exhaust unit are connected by an exhaust hose, and an exhaust solenoid valve and a vacuum pump of the exhaust unit are connected to a pressure switch for detecting a negative pressure in the water collecting trough. It is controlled by the controller.

サイホンブレーク配管系は排気ホースより太径の吸気用
配管をフロートあるいはフレーム上に設置し、該管を大
気に開放しうる電磁弁を設け、集水トラフ内の圧力を測
定するための圧力スイッチに接続される配管は集水トラ
フから直接又はサイホンブレーク配管から分岐して接続
する。
In the siphon break piping system, an intake pipe with a diameter larger than that of the exhaust hose is installed on the float or on the frame, and a solenoid valve that can open the pipe to the atmosphere is installed, and a pressure switch for measuring the pressure in the water collection trough is installed. The pipe to be connected is connected directly from the water collection trough or by branching from the siphon break pipe.

〔実施例〕〔Example〕

以下、本発明を図示の実施例に基づいて説明する。 Hereinafter, the present invention will be described based on the illustrated embodiments.

図において1は回分式活性汚泥法にて廃水を処理する処
理槽で、この所要容積を有する処理槽1内に水位変動に
追従して昇降する曝気装置2を設ける。この曝気装置2
は水位変動に対して昇降する1乃至複数個のフロート3,
3,3を曝気装置2のフレーム4に固定し、このフレーム
4に曝気機5とフロート全体の重心位置もしくは重心位
置近傍になるようにして帽函状の集水トラフ6とを設
け、このフロート3にて曝気装置2の全体は水位変動し
ても常に水面上に浮遊するようになす。
In the figure, reference numeral 1 is a treatment tank for treating wastewater by the batch activated sludge method, and an aeration device 2 which moves up and down following the fluctuation of the water level is provided in the treatment tank 1 having this required volume. This aeration device 2
Is one or more floats 3, which rises and falls in response to fluctuations in water level,
3 and 3 are fixed to a frame 4 of an aeration device 2, and an aerator 5 and a cap box-shaped water collecting trough 6 are provided on the frame 4 so as to be at or near the center of gravity of the float. At 3, the entire aeration apparatus 2 is always floated on the water surface even if the water level changes.

この曝気機5は各種のものが採用され、図示のものに限
定されることはない。図示の曝気機5は自吸式のもの
で、中空状の筒状カバー51内に駆動軸52を貫通させ、カ
バー外で、かつ常に水面下所定位置にあるようにして攪
拌羽根53を上記軸端に固定し、この軸の一端水面上にモ
ータ54を設け、このモータにて攪拌羽根53を回動させ、
廃水を攪拌する時、攪拌液中に生じる負圧を利用してカ
バー内あるいは中空状の駆動軸内を経て水面上の空気も
しくはガスを吸引し廃水中に吹き込むものである。フレ
ーム4に設けるフロート3は、その材質、形状、設置個
数に制限されるものでなく曝気機5を備えた曝気装置2
が水面上に安定して浮上しているものであればよい。
Various types of aeration machines 5 are adopted, and the aeration machine 5 is not limited to the illustrated one. The illustrated aerator 5 is of a self-priming type, in which a drive shaft 52 is penetrated into a hollow cylindrical cover 51, and the stirring blade 53 is provided outside the cover and always at a predetermined position below the water surface. It is fixed to the end, a motor 54 is provided on the water surface at one end of this shaft, and the stirring blade 53 is rotated by this motor,
When stirring the waste water, the negative pressure generated in the stirring liquid is used to suck air or gas on the water surface through the inside of the cover or the hollow drive shaft and blow it into the waste water. The float 3 provided on the frame 4 is not limited to its material, shape, and number of installations, and the aerator 2 including the aerator 5 is provided.
What is necessary is that it is stably floating on the surface of the water.

また、処理槽1の上部には架台Fを設け、この架台Fと
槽底間に1又は複数本のガイドロッドG,Gを架設し、こ
のガイドロッドGに前記曝気装置のフレーム4の一部例
えばフレーム4に突設したホルダー13を嵌挿支持させ、
曝気装置2が変動水位に追従して昇降しても処理槽1内
の所定位置にて支持されるようになす。
Further, a gantry F is provided on the upper part of the processing tank 1, and one or a plurality of guide rods G, G are installed between the gantry F and the bottom of the tank, and the guide rod G is part of the frame 4 of the aeration device. For example, by inserting and supporting the holder 13 protruding from the frame 4,
Even if the aeration device 2 moves up and down following the fluctuating water level, it is supported at a predetermined position in the processing tank 1.

集水トラフ6は帽函状をしており、伸縮屈伸可能なフレ
キシブルチューブ状の排水管7の上部に配設し、この排
水管7の下端は処理槽1の外部へ排水可能なように配設
された固定式の排水管8に接続される。帽函状の集水ト
ラフ6内には伸縮式排水管7の上端に一体に設けた直管
状の越流管9を挿入し、かつこの越流管9の越流堰部が
水面上少なくとも5〜10cmとなるようステーを介して上
記集水トラフ6に固定され、この集水トラフ6と越流管
9及び集水トラフ6とフレーム4とはそれぞれ固定され
る。そしてこの集水トラフ6はコップを上下逆にしたよ
うな形状で、その外周板下端は水面下少なくとも10〜15
cm程度浸漬するように固定し、これにより上澄水の排水
は集水トラフ6の外周板下端縁を越流し、集水トラフ内
にてしかも水面より5〜10cm上位にて開口した越流管上
端より排水管内へ排水され、水面にスカムが浮いていて
も水面から10cm以下の水深から集水してスカムを巻き込
まなようにするものである。
The water collecting trough 6 has a cap box shape, and is arranged on the upper part of a flexible tube-shaped drain pipe 7 that can be expanded and contracted, and the lower end of this drain pipe 7 is arranged so that it can be discharged to the outside of the treatment tank 1. It is connected to the fixed drainage pipe 8 provided. A straight tubular overflow pipe 9 integrally provided at the upper end of the telescopic drainage pipe 7 is inserted into the cap box-shaped water collection trough 6, and the overflow weir portion of the overflow pipe 9 is at least 5 on the water surface. It is fixed to the water collection trough 6 via a stay so as to be about 10 cm, and the water collection trough 6, the overflow pipe 9, and the water collection trough 6 and the frame 4 are fixed, respectively. The water collecting trough 6 has a shape like an upside down cup, and the lower end of the outer peripheral plate is at least 10 to 15 below the water surface.
It is fixed so as to be immersed in about cm, so that the drainage of the supernatant water overflows the lower edge of the outer peripheral plate of the collection trough 6, and the upper end of the overflow pipe opened in the collection trough and 5 to 10 cm above the water surface. Even if the scum floats to the drainage pipe and floats on the water surface, it collects water from a depth of 10 cm or less from the water surface to prevent the scum from being caught.

また、伸縮式排水管7は水位変動に追従して伸縮する
が、この場合円滑にかつ正確に行えるようにガイド装置
10が備えられる。
Also, the telescopic drainage pipe 7 expands and contracts following the water level fluctuation, but in this case, a guide device is provided so that it can be smoothly and accurately performed.
10 will be provided.

さらに、上記集水トラフ6の下部にはトラフ外径寸法と
同等もしくはそれ以上の大きさを有する水流ガイド板11
をほぼ水平になるようにして越流管9又は排水管7の外
周に設けて一体とする。このとき水流ガイド板11と集水
トラフ外周板下端縁との間は上澄水が排水時流水できる
適当な間隔が設けられる。
Further, a water flow guide plate 11 having a size equal to or larger than the outer diameter of the trough is provided under the water collecting trough 6.
Are provided on the outer circumference of the overflow pipe 9 or the drain pipe 7 so as to be substantially horizontal and integrated. At this time, an appropriate gap is provided between the water flow guide plate 11 and the lower edge of the outer peripheral plate of the water collecting trough so that the supernatant water can flow during drainage.

また、前記集水トラフ6には上澄水排水時、該トラフ内
を負圧にしてトラフ内水位を処理槽内水位より上昇さ
せ、越流管9よりサイフォン現象にて越流排水するため
の排水制御回路12が設けられる。
Further, when the supernatant water is drained to the water collection trough 6, a negative pressure is applied to the trough to raise the water level in the trough to a level higher than the water level in the treatment tank, and drain water for overflow drainage by the siphon phenomenon from the overflow pipe 9. A control circuit 12 is provided.

この排水制御回路12は第1図に詳示するように排気配管
系20とサイホンブレーク配管系30とより構成され、この
排気配管系20は集水トラフ6より排気ホース21を接続
し、この排気ホース21の先端に排気ユニット22を設け、
サイホンブレーク配管系は集水トラフ6に接続され、し
かもフレーム4に固定された排気ホース21より太径の吸
気用配管31と、この管31の先端部に設け、該管先端を大
気に開放可能とする電磁弁32とよりなる。
As shown in detail in FIG. 1, this drainage control circuit 12 is composed of an exhaust piping system 20 and a siphon break piping system 30. This exhaust piping system 20 is connected to an exhaust hose 21 from a water collection trough 6 An exhaust unit 22 is provided at the tip of the hose 21,
The siphon break piping system is connected to the water collection trough 6 and is provided at the tip end of this intake pipe 31 having a diameter larger than that of the exhaust hose 21 fixed to the frame 4, and the end of this pipe can be opened to the atmosphere. And a solenoid valve 32.

排気ユニット22には前記排気ホース21の先端にドレント
ラップ23を介して又は直接に電磁弁24を接続すると共
に、この電磁弁24に直接あるいは排気量調整弁25、流量
計26を介して真空ポンプ27を接続し、さらに集水トラフ
6より別の配管28を接続し、この管28の先端に圧力スイ
ッチ29を設け、この圧力スイッチ29、処理槽内に設けた
水位計33、電磁弁24、真空ポンプ27と制御装置40と電気
的に接続して構成される。
To the exhaust unit 22, a solenoid valve 24 is connected to the end of the exhaust hose 21 via a drain trap 23 or directly, and a vacuum pump is connected to the solenoid valve 24 directly or via an exhaust volume adjusting valve 25 and a flow meter 26. 27 is connected, and another pipe 28 is further connected from the water collection trough 6, a pressure switch 29 is provided at the tip of this pipe 28, and this pressure switch 29, a water level gauge 33 provided in the treatment tank, a solenoid valve 24, The vacuum pump 27 and the control device 40 are electrically connected to each other.

なお、サイホンブレーク配管系の電磁弁32も前記制御装
置40と電気的に接続される。また制御装置40と曝気機の
モータとも電気的に接続される。そしてこの排水制御回
路12は水上にすべて設置されるものである。
The solenoid valve 32 of the siphon break piping system is also electrically connected to the control device 40. The control device 40 and the motor of the aerator are also electrically connected. And this drainage control circuit 12 is installed all over the water.

上述の如く構成される廃水処理装置を用いて廃水の処理
を行う作用について以下説明する。
The operation of treating the wastewater using the wastewater treatment device configured as described above will be described below.

処理槽内に流入せしめた廃水(原水)を回分式活性汚泥
法にて処理するには、まず曝気機5 を運転し、攪拌羽根53の回動にて原水中に生じる負圧を
利用し空気を微細化して水中に吹き込みつつ攪拌して所
望の曝気を行なう。このとき越流管9の越流堰部が水面
上少なくとも5〜10cmとなるようにして、しかもその上
部から帽函状の集水トラフ6で覆うようにしているの
で、曝気工程では浮遊する汚泥が越流管9内に流れ込む
のを防止できる。すなわち処理水に汚泥が混入するのを
防止できる。このようにして一定時間曝気して回分式活
性汚泥法の処理が終了して、汚泥分を沈澱させた後、上
澄水を排水する場合、集水トラフ6内を排気して負圧に
すると、トラフ内の水位は上昇し、越流管上端より越流
し、排水されると共にサイフォン現象により連続的に排
水される。
To treat the wastewater (raw water) that has flowed into the treatment tank by the batch activated sludge method, first operate the aerator 5 and use the negative pressure generated in the raw water by the rotation of the stirring blades 53 to generate air. Is pulverized and stirred while being blown into water to perform desired aeration. At this time, since the overflow weir of the overflow pipe 9 is at least 5 to 10 cm above the water surface and is covered from above by the cap trough-shaped water collection trough 6, sludge floating in the aeration process Can be prevented from flowing into the overflow pipe 9. That is, it is possible to prevent the sludge from mixing into the treated water. In this way, when the batch activated sludge process is completed by aeration for a certain period of time and the sludge content is allowed to settle, and the supernatant water is drained, if the inside of the water collection trough 6 is exhausted to a negative pressure, The water level in the trough rises, overflows from the upper end of the overflow pipe, is drained, and is continuously drained by the siphon phenomenon.

このトラフ内の負圧は排気用電磁弁24を開いて真空用ポ
ンプ27を起動することにより排気ホース21を経て集水ト
ラフ6内の空気を吸引排出して行なう。この集水トラフ
内に大気圧より低い負圧が生じると該トラフ内の水位置
は上昇し、越流管9の上端より越流排出される。このよ
うに真空ポンプを起動して一定時間経過した時、サイホ
ンは形成されるがこれを圧力スイッチ29で検出すること
により、排気電磁弁24を閉じ、かつ真空ポンプ27も停止
させる。しかしこの時サイホンが形成されているので連
続的に排水が行なわれる。
The negative pressure in this trough is performed by suctioning and discharging the air in the water collection trough 6 via the exhaust hose 21 by opening the exhaust electromagnetic valve 24 and starting the vacuum pump 27. When a negative pressure lower than the atmospheric pressure is generated in the water collecting trough, the water position in the trough rises and is overflowed and discharged from the upper end of the overflow pipe 9. In this way, when the vacuum pump is started and a certain time has elapsed, a siphon is formed, but by detecting this with the pressure switch 29, the exhaust electromagnetic valve 24 is closed and the vacuum pump 27 is also stopped. However, since the siphon is formed at this time, drainage is continuously performed.

なお、圧力スイッチ29の設定圧力h(mmAq)は排水管7
の内径D(m)、処理槽の水位から水封部の頂部までの
距離H(m)に対し、 ただし、ho:越流堰の処理槽の水位に対する越流高さ(m
m)となるように設定することが望ましい。これによ
り、過大な圧力設定値とならないため、排気ユニット22
に水を吸引することなく、また真空ポンプ27を最小限必
要な時間だけ運転でき、省エネとなる。
The set pressure h (mmAq) of the pressure switch 29 is the drainage pipe 7
Inner diameter D (m) and the distance H (m) from the water level in the treatment tank to the top of the water seal part, However, ho: Overflow height (m in relation to the water level in the treatment tank of the overflow weir
It is desirable to set so that m). This prevents the pressure setting value from becoming too high, so the exhaust unit 22
It is possible to operate the vacuum pump 27 for a minimum required time without sucking water, and it is possible to save energy.

この上澄水の排水工程において排水にともない水位の低
下に追従して水面上に浮遊している曝気装置2も低下す
る。そして汚泥の界面位置に達し、汚泥界面が水流ガイ
ド板11下方の近傍となってもこの水流ガイド板11により
排水時の汚泥の巻き上げ、巻き込みを防止し、上澄水の
みの排水が行なえる。
In the process of draining the clear water, the aeration device 2 floating on the water surface also follows the drop of the water level with the drainage. Then, even when the sludge interface position is reached and the sludge interface is near the lower part of the water flow guide plate 11, the water flow guide plate 11 prevents the sludge from being rolled up and entrained during drainage, and only the supernatant water can be drained.

さらに排水時、水面にスカムが浮遊していても水面から
10cm以下の水深から集水排水しているのでスカムを巻き
込むことがない。
Furthermore, when draining water, even if scum floats on the water surface,
Since the water is collected and drained from a water depth of 10 cm or less, scum will not be involved.

そして、排水により水位が低下し、予め定めた低水位LW
Lに達すると水位計33の作動にてサイホンブレーク用電
磁弁32が開放される。この電磁弁32を予め定めた時間開
放しているとサイホンはブレークされ排水は停止される
ものである。
Then, the water level drops due to drainage, and the low water level LW
When reaching L, the solenoid valve 32 for siphon break is opened by the operation of the water level gauge 33. If the solenoid valve 32 is opened for a predetermined time, the siphon breaks and drainage is stopped.

〔発明の効果〕〔The invention's effect〕

本発明は以上説明したように構成されているので以下に
記載されるような効果を奏する。
Since the present invention is configured as described above, it has the following effects.

集水トラフに排気配管系とサイホンブレーク配管とを設
けて選択的に制御しているので上澄水の排水がサイホン
形成により排水できる。
Since an exhaust pipe system and a siphon break pipe are provided in the water collection trough and selectively controlled, the supernatant water can be drained by forming a siphon.

排気ホースをサイホンブレーク管と別に設けているの
で、設置場所を自由に選定できる。
Since the exhaust hose is provided separately from the siphon break pipe, the installation location can be freely selected.

サイホンブレーク配管系を太径とし、かつ曝気装置のフ
レームに設けているので短時間でサイホンをブレークす
ることができる。
Since the siphon break piping system has a large diameter and is installed in the frame of the aeration device, the siphon can be broken in a short time.

圧力スイッチに接続される配管を集水トラフより直接配
管接続しているので真空ポンプの脈動に影響を受け誤作
動することなく圧力スイッチは正常に作動する。
Since the pipe connected to the pressure switch is directly connected from the water collection trough, the pressure switch operates normally without being affected by the pulsation of the vacuum pump and without malfunction.

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

図面は本発明の実施例を示し、第1図は縦断正面図、第
2図は縦断側面図、第3図は平面図、第4図は集水トラ
フの説明図、第5図は同横断面図である。 1は処理槽、2は曝気装置、3はフロート、4はフレー
ム、5は曝気機、6は集水トラフ、7は排水管、11は水
流ガイド板、12は排水制御回路、20は排気配管系、21は
排気ホース、22は排気ユニット、24は電磁弁、27は真空
ポンプ、30はサイホンブレーク配管系、31は吸気用配
管、32は電磁弁、29は圧力スイッチ、40は制御装置。
Drawing shows an embodiment of the present invention, Fig. 1 is a vertical sectional front view, Fig. 2 is a vertical sectional side view, Fig. 3 is a plan view, Fig. 4 is an explanatory view of a water collecting trough, and Fig. 5 is the same cross section. It is a side view. 1 is a treatment tank, 2 is an aeration device, 3 is a float, 4 is a frame, 5 is an aerator, 6 is a water collecting trough, 7 is a drain pipe, 11 is a water flow guide plate, 12 is a drainage control circuit, and 20 is an exhaust pipe. System, 21 is an exhaust hose, 22 is an exhaust unit, 24 is a solenoid valve, 27 is a vacuum pump, 30 is a siphon break piping system, 31 is an intake pipe, 32 is a solenoid valve, 29 is a pressure switch, and 40 is a control device.

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】処理槽内の水位変動に対し追従して昇降す
るようにフロート付フレームに曝気機及び伸縮式の排水
管上端に越流管を設け、これを覆うようにして帽函状の
集水トラフを設けた廃水処理における上澄水排出制御装
置において、集水トラフに上澄水排出時サイホンを形成
するための排気配管系とサイホンブレーク配管系とを接
続し、かつこの各配管系の機器を制御装置にて制御する
ことを特徴とする廃水処理における上澄水排出制御装
置。
1. An aerator and an overflow pipe at the upper end of a telescopic drainage pipe are provided on a frame with a float so as to move up and down in response to fluctuations in the water level in the treatment tank, and a cap box-shaped cover is provided so as to cover the aeration machine. In a supernatant water discharge control device for wastewater treatment provided with a water collecting trough, an exhaust pipe system for forming a siphon at the time of discharging the supernatant water and a siphon break pipe system are connected to the water collecting trough, and equipment of each pipe system. And a control device for controlling the discharge of supernatant water in wastewater treatment.
【請求項2】排気配管系には集水トラフと排気ユニット
間を排気用ホースで接続し、かつ排気ユニットの排気用
電磁弁・真空ポンプを集水トラフ内の負圧を検出する圧
力スイッチに接続した制御装置にて制御するようになし
たことを特徴とする請求項1記載の廃水処理における上
澄水排出装置。
2. The exhaust pipe system is connected between the water collection trough and the exhaust unit with an exhaust hose, and the exhaust solenoid valve / vacuum pump of the exhaust unit is used as a pressure switch for detecting negative pressure in the water collection trough. The supernatant water discharger in wastewater treatment according to claim 1, wherein the controller is controlled by a connected controller.
【請求項3】サイホンブレーク配管系は排気ホースより
太径の吸気用配管をフロートあるいはフレーム上に設置
し、該管を大気に開放しうる電磁弁を設けたことを特徴
とする請求項1記載の廃水処理における上澄水排出制御
装置。
3. The siphon break piping system is characterized in that an intake pipe having a diameter larger than that of an exhaust hose is installed on a float or a frame, and a solenoid valve capable of opening the pipe to the atmosphere is provided. Control device for clear water discharge in wastewater treatment in Japan.
【請求項4】集水トラフ内の圧力を測定するための圧力
スイッチに接続される配管は集水トラフから直接又はサ
イホンブレーク配管から分岐して接続することを特徴と
する請求項2記載の廃水処理における上澄水排出制御装
置。
4. The wastewater according to claim 2, wherein the pipe connected to the pressure switch for measuring the pressure in the water collection trough is connected directly from the water collection trough or branched from the siphon break pipe. Clear water discharge control device in treatment.
JP63175358A 1988-07-13 1988-07-13 Clear water discharge control device in wastewater treatment Expired - Lifetime JPH0720589B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63175358A JPH0720589B2 (en) 1988-07-13 1988-07-13 Clear water discharge control device in wastewater treatment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63175358A JPH0720589B2 (en) 1988-07-13 1988-07-13 Clear water discharge control device in wastewater treatment

Publications (2)

Publication Number Publication Date
JPH0226693A JPH0226693A (en) 1990-01-29
JPH0720589B2 true JPH0720589B2 (en) 1995-03-08

Family

ID=15994680

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63175358A Expired - Lifetime JPH0720589B2 (en) 1988-07-13 1988-07-13 Clear water discharge control device in wastewater treatment

Country Status (1)

Country Link
JP (1) JPH0720589B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2619324B2 (en) * 1992-11-17 1997-06-11 薫 三橋 Fully automatic intermittent aeration device
KR100381575B1 (en) * 2000-09-27 2003-05-12 주식회사 환경비젼이십일 Plant for efficiency effluent of dissolved matter from the wastewater separated into solids and dissolved matter
JP2012132710A (en) * 2010-12-20 2012-07-12 Toshiba Corp Full water monitoring device of emergency core cooling system

Also Published As

Publication number Publication date
JPH0226693A (en) 1990-01-29

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