JPS6327832Y2 - - Google Patents

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Publication number
JPS6327832Y2
JPS6327832Y2 JP1984156360U JP15636084U JPS6327832Y2 JP S6327832 Y2 JPS6327832 Y2 JP S6327832Y2 JP 1984156360 U JP1984156360 U JP 1984156360U JP 15636084 U JP15636084 U JP 15636084U JP S6327832 Y2 JPS6327832 Y2 JP S6327832Y2
Authority
JP
Japan
Prior art keywords
scum
pipe
supernatant
overflow
discharge
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
Application number
JP1984156360U
Other languages
Japanese (ja)
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JPS6171295U (en
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Filing date
Publication date
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Priority to JP1984156360U priority Critical patent/JPS6327832Y2/ja
Publication of JPS6171295U publication Critical patent/JPS6171295U/ja
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Expired 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

Landscapes

  • Activated Sludge Processes (AREA)
  • Removal Of Floating Material (AREA)

Description

【考案の詳細な説明】[Detailed explanation of the idea] 【産業上の利用分野】[Industrial application field]

この考案は、単一の処理槽内で曝気・沈澱・排
出の工程から成るサイクルを繰り返して汚水処理
を行うバツチ式活性汚泥処理装置において、特
に、上澄液を排出するとともにスカムも確実に排
出できるスカム除去装置付デカンタに関するもの
である。
This idea is especially useful in batch-type activated sludge treatment equipment, which processes wastewater by repeating a cycle of aeration, sedimentation, and discharge in a single treatment tank. The present invention relates to a decanter equipped with a scum removing device.

【従来の技術】[Conventional technology]

一般に単一処理槽内のバツチ式活性汚泥処理装
置においては、沈澱工程後に上澄液を排出し、該
排出時において、上記処理槽内にスカムが浮遊し
ている場合には、そのスカムをも除去する必要が
ある。 このため、バツチ式活性汚泥処理装置において
も、一般的な汚泥処理装置の場合と同様に上澄液
排出装置と何らかのスカム除去手段を設ける必要
がある。 一般的な汚泥処理装置では、槽内の水位が略一
定か、または僅かに変動するだけであり、このた
め、スカム除去手段としては、バツフル併用によ
る固定スキマーや、水面積の少ない液面に浮かべ
るフローチングスキマー等が使用され、それなり
の効果を得ている。
Generally, in batch-type activated sludge treatment equipment in a single treatment tank, the supernatant liquid is discharged after the sedimentation process, and if there is scum floating in the treatment tank at the time of discharge, the scum is also removed. Needs to be removed. Therefore, even in the batch type activated sludge treatment apparatus, it is necessary to provide a supernatant liquid discharge device and some kind of scum removal means, as in the case of a general sludge treatment apparatus. In general sludge treatment equipment, the water level in the tank is approximately constant or only slightly fluctuates, so scum removal methods include a fixed skimmer combined with a buttful, or a floating skimmer on the liquid surface with a small water area. Floating skimmers and the like are being used with some success.

【考案が解決しようとする問題点】[Problem that the invention attempts to solve]

しかしながら、バツチ式活性汚泥処理装置の場
合、槽内水位が大きくは2m乃至3mも変動する
ため、水位変動が極めて少ない一般的は活性汚泥
処理装置を対象としたスキマーを単に転用したの
では、効果的なスカム回収が全く期待できないと
いう問題点があつた。 このため、バツチ式活性汚泥処理装置におい
て、上澄液排出装置については種々工夫が成され
てきたが、スカム除去手段については、上澄液排
出装置の場合と同様に非常に複雑な機構となり、
スペース的、コスト的にも問題が多く、さらに自
動化を図ると非常に高価になるため、現状ではあ
まり考慮されていないという問題点があつた。 この考案は上記のような問題点を解消するため
になされたもので、機構的に簡単な構成でありな
がら、広に槽内の液面に発生したスカムを、槽内
水位が大きく変動しても確実に回収・排出するこ
とができ、かつ、その回収・排出の自動化が図れ
ると共に、コスト的にも問題のないスカム除去装
置付デカンタを提供することを目的とする。
However, in the case of batch-type activated sludge treatment equipment, the water level in the tank fluctuates by as much as 2m to 3m, so simply reusing a skimmer that is generally intended for activated sludge treatment equipment, where water level fluctuations are extremely small, is not effective. There was a problem in that the scum collection could not be expected at all. For this reason, in batch-type activated sludge treatment equipment, various improvements have been made to the supernatant liquid discharge device, but the scum removal means is a very complicated mechanism similar to the supernatant liquid discharge device.
There are many problems in terms of space and cost, and further automation would be extremely expensive, so there are problems that are not considered much at present. This idea was devised to solve the problems mentioned above, and although it has a mechanically simple configuration, it can remove scum that has formed on the liquid level in the tank even when the water level in the tank fluctuates greatly. It is an object of the present invention to provide a decanter with a scum removing device that can reliably collect and discharge scum, automate the collection and discharge, and cause no cost problems.

【問題点を解決するための手段】[Means to solve the problem]

この考案に係るスカム除去装置付デカンタは、
流入汚水を受入れて活性汚泥処理を行う処理槽の
内底部側に横方向へ延びる軸パイプを軸廻り方向
へ回転可能に軸支し、この軸パイプに上澄液排出
パイプとスカム排出パイプとをそれぞれ所定間隔
で直角方向に連結し、それらの上澄液排出パイプ
とスカム排出パイプの各自由端部には、上記処理
槽内の液面に浮遊させる越流管を連結し、この越
流管内には、上記上澄液排出パイプで上記軸パイ
プ内に連通された上澄液流入路と、上記スカム排
出パイプで上記軸パイプ内を介して系外のスカム
排出系統に接続されたスカム流入路とを隔絶形成
し、上記上澄液流入路には、上記越流管の液面浮
遊状態で液面下に水没する上澄越流堰を形成した
上澄液流入口を設け、上記スカム流入路には、上
記処理槽内の水位低下によりその液面に追従して
下降する上記越流管の所定下降位置、例えばL.
W.Lより少し高い水面付近で液面下に水没するス
カム越流堰を形成したスカム流入口を設けたもの
である。
The decanter with a scum removal device according to this invention is
A shaft pipe extending laterally is rotatably supported on the inner bottom side of a treatment tank that receives inflow sewage and performs activated sludge treatment, and a supernatant liquid discharge pipe and a scum discharge pipe are connected to this shaft pipe. The supernatant liquid discharge pipe and the scum discharge pipe are connected at right angles at predetermined intervals, and each free end of the supernatant liquid discharge pipe and the scum discharge pipe is connected to an overflow pipe that floats on the liquid level in the processing tank. The supernatant liquid inflow path is connected to the shaft pipe by the supernatant liquid discharge pipe, and the scum inflow path is connected to the scum discharge system outside the system through the shaft pipe by the scum discharge pipe. The supernatant liquid inlet is provided with a supernatant liquid inlet formed with a supernatant overflow weir that is submerged below the liquid surface while the liquid surface of the overflow pipe is floating, and the above-mentioned scum inflow A predetermined lowering position of the overflow pipe, for example L.
It is equipped with a scum inlet that forms a scum overflow weir that is submerged below the liquid level near the water level, which is slightly higher than the WL.

【作用】[Effect]

この考案におけるスカム除去装置付デカンタ
は、処理槽内での曝気・沈澱工程後における上澄
液の排出に際し、軸パイプを回動させて処理槽内
の高水位(H.W.L)液面で越流管を浮遊させる
と、この浮遊状態で越流管の上澄越流堰が水没す
ることにより、この上澄越流堰を有する上澄液流
入口から上澄液流入路に上澄液が流入し、次い
で、その流入上澄液は上澄液排出パイプを流下
し、軸パイプ内を通つて系外に排出される。この
とき、上記越流管のスカム越流堰は液面上方に保
持されることにより、スカム流入口からスカム流
入路に上澄液が流入するようなことはない。 このような上澄液の排出により、処理槽内の水
位が順次低下し、その液面に追従して上記越流管
も下降することにより、該越流管のスカム越流堰
が漸次液面に近づき、上記処理槽内が低水位(L.
W.L)付近になると、上記スカム越流堰が上記上
澄越流堰と略同じ高さとなつて共に液面下で水没
する。このため、上記処理槽内の低水位(L.W.
L)付近の液面でスカムがスカム流入口からスカ
ム流入路に流入し、流入したスカムはスカム排出
パイプを流下して上記軸パイプ内のスカム排出経
路を通つて系外に排出される。これと同時に、上
澄液流入口からは上澄液が流入し、該上澄液は上
述した上澄液排出経路を通つて系外に排出され
る。
The decanter with a scum removal device of this invention rotates the shaft pipe to drain the overflow pipe at the high water level (HWL) in the treatment tank when discharging the supernatant liquid after the aeration and precipitation processes in the treatment tank. When suspended, the supernatant overflow weir of the overflow pipe is submerged in water, and the supernatant fluid flows into the supernatant fluid inlet channel from the supernatant fluid inlet having the supernatant overflow weir. Then, the incoming supernatant liquid flows down the supernatant liquid discharge pipe, passes through the shaft pipe, and is discharged to the outside of the system. At this time, the scum overflow weir of the overflow pipe is held above the liquid level, so that the supernatant liquid does not flow into the scum inflow path from the scum inflow port. Due to the discharge of such supernatant liquid, the water level in the treatment tank gradually decreases, and the overflow pipe also descends following the liquid level, so that the scum overflow weir of the overflow pipe gradually lowers the liquid level. , and the water level in the treatment tank is low (L.
Near WL), the scum overflow weir becomes approximately at the same height as the above-mentioned skimming overflow weir, and both are submerged below the liquid level. For this reason, the low water level (LW) in the treatment tank is
Scum flows into the scum inflow path from the scum inlet at the liquid level near L), and the inflowing scum flows down the scum discharge pipe and is discharged out of the system through the scum discharge path in the shaft pipe. At the same time, supernatant liquid flows in from the supernatant liquid inlet, and the supernatant liquid is discharged out of the system through the above-mentioned supernatant liquid discharge path.

【実施例】【Example】

以下、この考案の一実施例を図面に基づいて説
明する。 この考案に係るデカンタ1は、第1図および第
2図に示すように、曝気工程と沈澱工程および排
出工程のサイクルを繰り返して活性汚泥処理を行
う単一の処理槽10内に装備されている。 即ち、上記デカンタ1は、上記処理槽10の底
部側で軸廻り方向へ回転可能に軸支されて横方向
(図示例では略水平方向)に延びる軸パイプ2を
有している。 この軸パイプ2は上澄液排出路を形成するもの
で、一端に上澄液排出口2aを有して回動手段7
により軸廻り方向に回動できるようになつてい
る。 かかる軸パイプ2には、その直角方向に延びる
アーム状をなした複数の排出パイプ3が所定の間
隔で一体的に連結されている。 更に詳しく述べると、上記排出パイプ3は上澄
液排出パイプ3aとスカム排出パイプ3bとから
成り、スカム排出パイプ3bは上記軸パイプ2内
に挿通された水平管部2bを有している。 この水平管部2bは上記軸パイプ2内で上澄液
排出口2aの反対側に延びてその軸パイプ2内で
スカム排出経路を形成している。尚、上記軸パイ
プ2の他端部は上記水平管部2bとの間で閉塞さ
れている。 従つて、図示例の上記軸パイプ2は上記水平管
部2bの挿通部分が二重管構造となつている。 このような上澄液排出パイプ3aとスカム排出
パイプ3bは、上述のように軸パイプ2と略直角
に一体連結されているため、該軸パイプ2を中心
として上下方向へスイングできるようになつてい
る。 そして、上澄液排出パイプ3aとスカム排出パ
イプ3bの各自由端部には、越流管4が水平方向
に連結されている。 この越流管4内には、第1図〜第6図に示すよ
うに、仕切り部4aによつて上澄液流入路5とス
カム流入路6とが隔絶形成されている。 ここで、上記上澄液流入路5は上記上澄液排出
パイプ3aによつて上記軸パイプ2内に連通さ
れ、かつ、上記スカム流入路6には上記スカム排
出パイプ3bが連通されている。 また、上記越流管4には、上記軸パイプ2に近
い側の上澄越流堰5aを有して上澄液流入路5に
連通する上澄液流入口5bと、上記軸パイプ2に
遠い側のスカム越流堰6aを有してスカム流入路
6に連通するスカム流入口6bとが設けられてい
る。 これらの上澄液流入口5bとスカム流入口6b
は、上記越流管4の所定個所を切欠することによ
り形成されている。 この場合、処理槽10内が如何なる水位であつ
ても、その液面付近で上記上澄越流堰5aが水没
するように、該上澄越流堰5aは形成されてい
る。 また、上記スカム越流堰6aは、上記上澄越流
堰5aとの位置関係において、上記処理槽10内
の水位低下に伴う上記越流管4の下降により液面
に漸次近づき、該越流管4の所定下降位置、例え
ばL.W.Lより少し高い水面付近で上記上澄越流堰
5aと同じ高さとなつて水没するように形成され
ている。 このような越流管4の両端部には、該越流管4
に上澄越流堰5a側の外方で平行するスカムバツ
フルを兼ねたフロート8の両端部が支持腕9で上
下揺動自在に連結され、そのフロート8によつ
て、液面上で浮遊するスカムが上澄越流堰5aに
流入するのを防止している。 次に、動作について説明する。 処理槽10内では、曝気工程と沈澱工程および
デカンタ1により上澄液を排出させる排出工程と
を1サイクルとして流入汚水の活性汚泥処理を行
う。尚、処理槽10内の沈澱汚泥は適当な時期に
引き抜かれる。 このような活性汚泥処理装置において、上記排
出工程では、回動手段7により軸パイプ2を回動
させてデカンタ1を第2図に一点鎖線で示す上限
位置から同図に実線で示す使用位置まで下降させ
ることにより、処理槽10における高水位(H.
W.L)の液面にフロート8が浮遊し、越流管4は
第1図および第5図に示すように上澄越流堰5a
がその液面付近で水没し、且つスカム越流堰6a
が液面上方に突出位置した状態に保持される。 従つて、この状態では、上記処理槽10内にお
ける越流管4とフロート8との間の上澄液が上澄
越流堰5aを越流して上澄液流入口5bから上澄
液流入路5に流入する。この場合、スカム越流堰
6aは上述の如く液面上方に保持されているた
め、スカム流入口6bからスカム流入路6に上澄
液が流入するようなことはない。 そして、上澄液流入路5内に流入した上澄液
は、その系統の上澄液排出パイプ3aを流下して
軸パイプ2内に至り、該軸パイプ2を通つて上澄
液排出口2aから系外に排出される。 このような上澄液の排出によつて、上記処理槽
10内の水位が順次低下し、これに伴つて、その
液面と共にデカンタ1が軸パイプ2を中心とする
円弧運動により下降する。 この下降過程において、上記スカム越流堰6a
は液面に漸次近づく方向に変位し、上記処理槽1
0内の液面が低水位(L.W.L)付近になると、上
記越流管4は第2図の二点鎖線および第6図に示
す状態に変位し、この状態では、スカム越流堰6
aが上澄越流堰5aと略同じ高さとなつて、それ
らは共に液面下に水没する。 そして、処理槽10内の液面が低水位(L.W.
L)付近になると、その液面に浮遊するスカムが
上記スカム越流堰6aを越流してスカム流入口6
bからスカム流入路6内に流入し、次いで、その
系統のスカム排出パイプ3bを流下して軸パイプ
2内の水平管部2b(スカム排出経路)を通つて
系外に排出される。 これと同時に、処理槽10内の低水位(L.W.
L)付近の上澄液も上澄越流堰5aを越流して上
澄液流入路5内に流入し、上述のように軸パイプ
2内を流通して系外に排出される。 従つて、処理槽10の低水位(L.W.L)付近で
は、上澄液とスカムの両方がそれぞれ専用の排出
経路を通つて同時に排出されることとなる。 そして、上記デカンタ1は、処理槽10内のL.
W.Lに達した時点で再び第2図に一点鎖線で示す
上限位置に復帰する。 ここで、スカム排出を効果的に行うためには、
上澄液の排出をL.W.Lでストツプし、スカムはも
う少し下のL.L.W.Lまで排出し、デカンタ1はL.
L.W.Lで作動して前記上限位置に復帰させること
が好ましく、このようなことを行うことも可能で
あり、また、上澄液の排出を必要に応じてL.W.L
の少し上でストツプさせることも可能である。 尚、上記実施例において、デカンタ1はスカム
が十分排出できるようにL.W.Lよりもつと低い位
置まで下降させるようにしてもよい。また、上記
デカンタ1におけるスカム排出系統に弁を設け、
この弁の開閉によつてスカムの排出を任意に操作
できるようにしてもよい。更に、上記上澄越流堰
5aおよびスカム越流堰6aは、その何れか一
方、または両方に高さ調整機構を設けるか、L.
W.L付近を調整可能とすることによつてスカム排
出量を調整できるようにしてもよい。 この場合、その調整を電動または手動で調整自
在とし、平常時はL.W.Lでスカム排出が起こらな
いようにし、必要時にのみスカムが排出できるよ
うにするとよい。 第7図〜第9図には他の実施例を示す。この実
施例における前実施例との相違点は、越流管4内
を径方向の仕切り部4aで仕切り、これによつ
て、上記越流管4内の軸方向にそれぞれ複数の上
澄液流入路5とスカム流入路6とを隔絶形成した
点であり、その他は前実施例の場合と同じであ
る。従つて、この実施例にあつても、前実施例の
場合と同様の作用結果が得られる。
An embodiment of this invention will be described below with reference to the drawings. As shown in FIGS. 1 and 2, the decanter 1 according to this invention is installed in a single treatment tank 10 that performs activated sludge treatment by repeating a cycle of an aeration process, a settling process, and a discharge process. . That is, the decanter 1 has a shaft pipe 2 that is rotatably supported on the bottom side of the processing tank 10 in the axial direction and extends laterally (substantially horizontally in the illustrated example). This shaft pipe 2 forms a supernatant liquid discharge passage, has a supernatant liquid discharge port 2a at one end, and has a rotating means 7.
It can be rotated around the axis. A plurality of arm-shaped discharge pipes 3 extending perpendicularly to the shaft pipe 2 are integrally connected to the shaft pipe 2 at predetermined intervals. More specifically, the discharge pipe 3 is composed of a supernatant liquid discharge pipe 3a and a scum discharge pipe 3b, and the scum discharge pipe 3b has a horizontal pipe portion 2b inserted into the shaft pipe 2. This horizontal pipe portion 2b extends within the shaft pipe 2 to the opposite side of the supernatant liquid discharge port 2a, and forms a scum discharge path within the shaft pipe 2. The other end of the shaft pipe 2 is closed with the horizontal pipe section 2b. Therefore, the shaft pipe 2 in the illustrated example has a double pipe structure in the portion through which the horizontal pipe portion 2b is inserted. As described above, the supernatant liquid discharge pipe 3a and the scum discharge pipe 3b are integrally connected to the shaft pipe 2 at a substantially right angle, so that they can swing vertically around the shaft pipe 2. There is. An overflow pipe 4 is horizontally connected to each free end of the supernatant liquid discharge pipe 3a and the scum discharge pipe 3b. In this overflow pipe 4, as shown in FIGS. 1 to 6, a supernatant fluid inflow path 5 and a scum inflow path 6 are separated from each other by a partition portion 4a. Here, the supernatant fluid inflow path 5 is communicated with the shaft pipe 2 through the supernatant fluid discharge pipe 3a, and the scum inflow path 6 is communicated with the scum discharge pipe 3b. The overflow pipe 4 also has a supernatant overflow weir 5a on the side closer to the shaft pipe 2, and a supernatant liquid inlet 5b communicating with the supernatant liquid inflow path 5, and A scum inlet 6b that has a scum overflow weir 6a on the far side and communicates with the scum inflow path 6 is provided. These supernatant liquid inlet 5b and scum inlet 6b
is formed by cutting out a predetermined portion of the overflow pipe 4. In this case, the supernatant overflow weir 5a is formed so that the supernatant overflow weir 5a is submerged near the liquid level no matter what the water level is in the processing tank 10. In addition, in the positional relationship with the supernatant overflow weir 5a, the scum overflow weir 6a gradually approaches the liquid level due to the lowering of the overflow pipe 4 as the water level in the treatment tank 10 decreases, and the overflow It is formed to be submerged at a predetermined lowering position of the pipe 4, for example near the water level slightly higher than LWL, at the same height as the above-mentioned supernatant overflow weir 5a. At both ends of such an overflow pipe 4, an overflow pipe 4 is provided.
Both ends of a float 8, which also serves as a scum baffle and is parallel to the outside of the supernatant overflow weir 5a, are connected by support arms 9 so as to be able to swing up and down, and the float 8 allows the scum floating on the liquid surface to be moved upwardly and downwardly. This prevents water from flowing into the supernatant overflow weir 5a. Next, the operation will be explained. In the treatment tank 10, activated sludge treatment of the inflowing sewage is performed, with the aeration process, the settling process, and the discharge process of discharging the supernatant liquid using the decanter 1 as one cycle. Incidentally, the settled sludge in the treatment tank 10 is drawn out at an appropriate time. In such an activated sludge treatment apparatus, in the discharge step, the shaft pipe 2 is rotated by the rotating means 7 to move the decanter 1 from the upper limit position shown by the dashed line in FIG. 2 to the use position shown by the solid line in the same figure. By lowering the water level, the high water level (H.
A float 8 floats on the liquid surface of WL), and the overflow pipe 4 is connected to the supernatant overflow weir 5a as shown in FIGS. 1 and 5.
is submerged near the liquid level, and the scum overflow weir 6a
is held in a position protruding above the liquid level. Therefore, in this state, the supernatant liquid between the overflow pipe 4 and the float 8 in the processing tank 10 overflows the supernatant overflow weir 5a and flows from the supernatant liquid inlet 5b to the supernatant liquid inflow path. 5. In this case, since the scum overflow weir 6a is held above the liquid level as described above, the supernatant liquid will not flow into the scum inflow path 6 from the scum inflow port 6b. Then, the supernatant liquid that has flowed into the supernatant liquid inflow path 5 flows down the supernatant liquid discharge pipe 3a of that system, reaches the inside of the shaft pipe 2, and passes through the shaft pipe 2 to the supernatant liquid discharge port 2a. is discharged from the system. Due to such discharge of the supernatant liquid, the water level in the processing tank 10 gradually decreases, and the decanter 1 descends along with the liquid level by an arcuate movement around the shaft pipe 2. In this descending process, the scum overflow weir 6a
is displaced in a direction that gradually approaches the liquid level, and the treatment tank 1
When the liquid level in 0 becomes near the low water level (LWL), the overflow pipe 4 is displaced to the state shown by the two-dot chain line in FIG. 2 and in FIG. 6, and in this state, the scum overflow weir 6
a is at approximately the same height as the supernatant overflow weir 5a, and both are submerged below the liquid level. Then, the liquid level in the treatment tank 10 is at a low water level (LW
L), the scum floating on the liquid surface overflows the scum overflow weir 6a and the scum inlet 6a.
scum flows into the scum inflow path 6 from the scum inflow path 6, then flows down the scum discharge pipe 3b of the system, passes through the horizontal pipe portion 2b (scum discharge path) in the shaft pipe 2, and is discharged to the outside of the system. At the same time, the low water level (LW) in the treatment tank 10
The supernatant liquid near L) also overflows the supernatant overflow weir 5a, flows into the supernatant liquid inflow path 5, flows through the shaft pipe 2 as described above, and is discharged to the outside of the system. Therefore, near the low water level (LWL) of the treatment tank 10, both the supernatant liquid and the scum are simultaneously discharged through their respective dedicated discharge paths. The decanter 1 is connected to the L.
When it reaches WL, it returns to the upper limit position shown by the dashed line in FIG. 2. In order to effectively remove scum,
Discharge of the supernatant liquid is stopped at LWL, scum is discharged to LLWL a little lower, and decanter 1 is stopped at L.
It is preferable to operate at LWL to return to the upper limit position, and it is also possible to do this, and also to drain the supernatant liquid at LWL as necessary.
It is also possible to stop at a point slightly above . In the above embodiment, the decanter 1 may be lowered to a position lower than LWL so that the scum can be sufficiently discharged. Further, a valve is provided in the scum discharge system in the decanter 1,
Scum discharge may be arbitrarily controlled by opening and closing this valve. Furthermore, either one or both of the above-mentioned skimming overflow weir 5a and scum overflow weir 6a is provided with a height adjustment mechanism, or the L.
The amount of scum discharged may be adjusted by making the area around WL adjustable. In this case, it is recommended that the adjustment be made electrically or manually so that scum is not discharged from the LWL during normal times, and scum can be discharged only when necessary. Other embodiments are shown in FIGS. 7-9. The difference between this embodiment and the previous embodiment is that the inside of the overflow pipe 4 is partitioned by a radial partition portion 4a, which allows a plurality of supernatant liquids to flow in each of the overflow pipes 4 in the axial direction. The difference is that the passage 5 and the scum inflow passage 6 are formed to be separated from each other, and other aspects are the same as in the previous embodiment. Therefore, even in this embodiment, the same operational results as in the previous embodiment can be obtained.

【考案の効果】[Effect of the idea]

以上のように、この考案によれば、処理槽内の
液面に浮遊させ、該液面水位の変動に追従して昇
降する1つの越流管によつて、上澄液とスカムを
個々に区分して回収・排出することができるの
で、処理槽内の水位が大きく変動しても、その変
動に関係なく上澄液とスカムを確実に区分して自
動的に効率よく回収・排出することができ、しか
も、構成が頗る簡単なため、スペース的およびコ
スト的な問題もなく、バツチ式活性汚泥処理装置
に好適なスカム除去装置付デカンタを提供できる
という効果がある。
As described above, according to this invention, the supernatant liquid and the scum are individually separated by a single overflow pipe that floats on the liquid level in the treatment tank and moves up and down following fluctuations in the liquid level. Since it can be collected and discharged separately, even if the water level in the treatment tank fluctuates greatly, the supernatant liquid and scum can be reliably separated and automatically and efficiently collected and discharged regardless of the fluctuations. Furthermore, since the structure is extremely simple, there are no space or cost problems, and there is an effect that a decanter with a scum removal device suitable for batch type activated sludge treatment equipment can be provided.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図はこの考案の一実施例によるスカム除去
装置付デカンタの平面図、第2図はその動作説明
を兼ねた概略的な側面図、第3図は同要部の拡大
断面図、第4図は越流管の拡大平面図、第5図は
第2図の実線状態における第4図の−線断面
図、第6図は第2図の二点鎖線状態における第4
図の−線断面図、第7図は他の実施例に係る
越流管の平面図、第8図は第7図の−線断面
図、第9図は第7図の−線断面図である。 図において、2は軸パイプ、3aは上澄液排出
パイプ、3bはスカム排出パイプ、4は越流管、
5は上澄液流入路、5aは上澄越流堰、5bは上
澄液流入口、6はスカム流入路、6aはスカム越
流堰、6bはスカム流入口である。
Fig. 1 is a plan view of a decanter with a scum removing device according to an embodiment of the invention, Fig. 2 is a schematic side view that also serves as an explanation of its operation, Fig. 3 is an enlarged sectional view of the main parts, and Fig. 4 The figure is an enlarged plan view of the overflow pipe, FIG. 5 is a sectional view taken along the line - - in FIG.
Fig. 7 is a plan view of an overflow pipe according to another embodiment, Fig. 8 is a sectional view taken along the - line in Fig. 7, and Fig. 9 is a sectional view taken along the - line in Fig. 7. be. In the figure, 2 is a shaft pipe, 3a is a supernatant liquid discharge pipe, 3b is a scum discharge pipe, 4 is an overflow pipe,
5 is a supernatant liquid inlet, 5a is a supernatant overflow weir, 5b is a supernatant liquid inlet, 6 is a scum inflow path, 6a is a scum overflow weir, and 6b is a scum inlet.

Claims (1)

【実用新案登録請求の範囲】 (1) 流入汚水を受入れて活性汚泥処理を行う処理
槽の内底部側に横方向へ延びる軸パイプを軸廻
り方向へ回転可能に軸支し、この軸パイプに上
澄液排出パイプとスカム排出パイプのそれぞれ
を所定間隔で直角方向に連結し、それらの上澄
液排出パイプとスカム排出パイプの各自由端部
に跨がつて連結され、上記処理槽内の液面に浮
遊させる越流管を備え、この越流管の内部に
は、上記上澄液排出パイプで上記軸パイプ内に
連通された上澄液流入路と、上記スカム排出パ
イプで上記軸パイプ内のスカム排出経路に接続
されたスカム流入路とが隔絶形成され、上記上
澄液流入路は、上記越流管の液面浮遊状態で液
面下に水没する上澄越流堰を形成した上澄液流
入口を有し、上記スカム流入路は、上記処理槽
内の水位低下に伴う上記越流管の下降により液
面に漸次近づいて該越流管の所定下降位置で液
面下に水没するスカム越流堰を形成したスカム
流入口を有していることを特徴とするスカム除
去装置付デカンタ。 (2) 上記越流管には、その上澄液流入口側の外方
に位置するスカムバツフルを兼ねたフロートが
連結されていることを特徴とする実用新案登録
請求の範囲第1項記載のスカム除去装置付デカ
ンタ。
[Scope of Claim for Utility Model Registration] (1) A shaft pipe extending laterally at the inner bottom side of a treatment tank that receives inflow sewage and performs activated sludge treatment is rotatably supported in the direction of the axis, and The supernatant liquid discharge pipe and the scum discharge pipe are connected in a perpendicular direction at predetermined intervals, and the liquid in the processing tank is connected by spanning the free ends of the supernatant liquid discharge pipe and the scum discharge pipe. An overflow pipe is provided to float the scum on the surface, and inside the overflow pipe there is a supernatant fluid inflow channel that communicates with the shaft pipe through the supernatant fluid discharge pipe, and a supernatant fluid inflow channel that communicates with the shaft pipe through the scum discharge pipe. The scum inflow path connected to the scum discharge path of the overflow pipe is separated from the scum inflow path, and the supernatant liquid inflow path is separated from the scum inflow path connected to the scum discharge path of the overflow pipe. The scum inflow path has a clear liquid inlet, and as the overflow pipe descends as the water level in the processing tank decreases, the scum inflow path gradually approaches the liquid level and is submerged below the liquid level at a predetermined lowering position of the overflow pipe. A decanter with a scum removal device, characterized in that it has a scum inlet in which a scum overflow weir is formed. (2) The scum according to claim 1 of the utility model registration claim, characterized in that the overflow pipe is connected to a float that also serves as a scum buttful and is located outside of the supernatant inlet side of the overflow pipe. Decanter with removal device.
JP1984156360U 1984-10-18 1984-10-18 Expired JPS6327832Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1984156360U JPS6327832Y2 (en) 1984-10-18 1984-10-18

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1984156360U JPS6327832Y2 (en) 1984-10-18 1984-10-18

Publications (2)

Publication Number Publication Date
JPS6171295U JPS6171295U (en) 1986-05-15
JPS6327832Y2 true JPS6327832Y2 (en) 1988-07-27

Family

ID=30714363

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1984156360U Expired JPS6327832Y2 (en) 1984-10-18 1984-10-18

Country Status (1)

Country Link
JP (1) JPS6327832Y2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPWO2010046960A1 (en) * 2008-10-20 2012-03-15 生田 尚之 Container type water purification system
JP5677480B2 (en) * 2013-02-14 2015-02-25 中国電力株式会社 Float collection device

Also Published As

Publication number Publication date
JPS6171295U (en) 1986-05-15

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