JPS6221354Y2 - - Google Patents

Info

Publication number
JPS6221354Y2
JPS6221354Y2 JP1982029194U JP2919482U JPS6221354Y2 JP S6221354 Y2 JPS6221354 Y2 JP S6221354Y2 JP 1982029194 U JP1982029194 U JP 1982029194U JP 2919482 U JP2919482 U JP 2919482U JP S6221354 Y2 JPS6221354 Y2 JP S6221354Y2
Authority
JP
Japan
Prior art keywords
chamber
contact aeration
guide tube
separation
separation chamber
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
JP1982029194U
Other languages
Japanese (ja)
Other versions
JPS58132593U (en
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 filed Critical
Priority to JP1982029194U priority Critical patent/JPS58132593U/en
Publication of JPS58132593U publication Critical patent/JPS58132593U/en
Application granted granted Critical
Publication of JPS6221354Y2 publication Critical patent/JPS6221354Y2/ja
Granted legal-status Critical Current

Links

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

  • Biological Treatment Of Waste Water (AREA)
  • Treatment Of Biological Wastes In General (AREA)

Description

【考案の詳細な説明】 この考案は接触曝気室の汚泥濃度を調節できる
浄化槽の改良に関する。
[Detailed description of the invention] This invention relates to an improvement of a septic tank that can adjust the sludge concentration in the contact aeration chamber.

従来から接触曝気法による汚水浄化処理装置で
は効果的な処理を行うために、曝気室内の汚泥濃
度が高くなつたとき、曝気室内の混合液をポンプ
等で汲み取つて前段の沈殿分離室等へ返送し濃度
調整を行つている。もし、上記作業を怠れば、曝
気室内の混合液濃度が増大して、沈殿上澄水に多
量の固形物が含まれるようになり、放流水の水質
が悪化する。また、曝気室内の撹拌力を利用して
自動的に汚泥を返送することも提案されている
が、この場合返送量の調整が困難であつた。
Conventionally, in sewage purification treatment equipment using the contact aeration method, in order to perform effective treatment, when the sludge concentration in the aeration chamber becomes high, the mixed liquid in the aeration chamber is pumped up using a pump, etc., and sent to the previous stage, such as a sedimentation separation chamber. It was sent back and the concentration was adjusted. If the above operations are neglected, the concentration of the mixed liquid in the aeration chamber will increase, the supernatant water will contain a large amount of solid matter, and the quality of the effluent will deteriorate. It has also been proposed to automatically return sludge using the stirring force in the aeration chamber, but in this case it has been difficult to adjust the amount of return.

この考案は上記欠点を解決し、ポンプ等の手段
を必要とせずに、接触曝気室内に立設された案内
筒上方の曝気装置の吐出口からの混合液の流れを
利用することによつて、分離室または独立した汚
泥貯留室へ接触曝気室内の汚泥の返送を行い、し
かも吐出口の方向を回転調整することによつて汚
泥の返送量の調整ができるので、安定した処理が
行なえる浄化槽を提供することを目的とする。
This invention solves the above-mentioned drawbacks by utilizing the flow of the mixed liquid from the discharge port of the aeration device above the guide cylinder installed in the contact aeration chamber, without requiring means such as a pump. The sludge in the contact aeration chamber is returned to the separation chamber or an independent sludge storage chamber, and the amount of sludge returned can be adjusted by rotating the direction of the discharge port, creating a septic tank that can perform stable treatment. The purpose is to provide.

以下、この考案の一実施例について図面を参照
して説明する。
An embodiment of this invention will be described below with reference to the drawings.

第1図に示すように、例えばFRP等で形成さ
れた浄化槽本体1の内部は2つの仕切壁2および
3によつて分離室4、接触曝気室5および沈殿室
6とに区画されている。そして、該浄化槽本体1
の側壁には分離室4に連通する汚水の流入管7と
沈殿室6に連通する流出管8が設けられている。
そして上記分離室4と接触曝気室5とは汚泥返送
口も兼ねる移流管9によつて連通され、また接触
曝気室5と沈殿室6とはその仕切壁3の下端と槽
底との間に残された開口10によつて、連通され
ている。
As shown in FIG. 1, the inside of a septic tank main body 1 made of, for example, FRP is divided by two partition walls 2 and 3 into a separation chamber 4, a contact aeration chamber 5, and a precipitation chamber 6. And the septic tank main body 1
An inflow pipe 7 for sewage that communicates with the separation chamber 4 and an outflow pipe 8 that communicates with the settling chamber 6 are provided on the side wall of the tank.
The separation chamber 4 and the contact aeration chamber 5 are communicated by an advection pipe 9 which also serves as a sludge return port, and the contact aeration chamber 5 and the settling chamber 6 are connected between the lower end of the partition wall 3 and the bottom of the tank. They are communicated through the remaining opening 10.

上記接触曝気室5の上方蓋板部分には第1図、
第2図に示すように電動機11が設置され、その
回転軸12が接触曝気室5の液面に向けて張出さ
れている。そしてその先端にはインペラ13が取
付けられていて、液面下部位で回転されるように
なつている。上記回転軸12の下方には、これと
同軸的に案内筒14が設けられている。この案内
筒14に対して回転自在に挿着されたドラフト管
15が電動機11の枠体に固定され、インペラを
囲むように配置され曝気装置を形成している。こ
の案内筒14は仕切壁2と仕切壁3との間に装着
された材16によつて支持され、インペラ13
の回転によつて、案内筒14の下端開口から液を
揚上するようになつている。
The upper cover plate of the contact aeration chamber 5 is shown in FIG.
As shown in FIG. 2, an electric motor 11 is installed, and its rotating shaft 12 extends toward the liquid level of the contact aeration chamber 5. An impeller 13 is attached to its tip and rotated below the liquid level. A guide cylinder 14 is provided below the rotating shaft 12 and coaxially therewith. A draft pipe 15 rotatably inserted into the guide tube 14 is fixed to the frame of the electric motor 11, and is arranged to surround the impeller to form an aeration device. This guide cylinder 14 is supported by a member 16 installed between the partition walls 2 and 3, and the impeller 13
By the rotation of the guide tube 14, liquid is lifted up from the lower end opening of the guide tube 14.

また上記ドラフト管15は第2図から第4図に
示すように、その上端部周壁に複数の吐出口17
が設けられていると共に、案内筒14に対して回
転自在に設置されているので、吐出口17の移流
管9に対する方向を回転調整して、接触曝気室5
のSSを移流管9を介して分離室4に返送する量
を調整できるようになつている。
Further, as shown in FIGS. 2 to 4, the draft pipe 15 has a plurality of discharge ports 17 on its upper end peripheral wall.
is provided and is rotatably installed with respect to the guide tube 14, so the direction of the discharge port 17 with respect to the advection tube 9 can be adjusted by rotation, and the contact aeration chamber 5
The amount of SS returned to the separation chamber 4 via the advection pipe 9 can be adjusted.

次にこの考案の動作について説明する。 Next, the operation of this invention will be explained.

処理すべき汚水は流入管7から分離室4内へ流
入し、沈殿分離が行なわれた後、移流管9から接
触曝気室5へ流入する。この接触曝気室5では、
インペラ13の回転によつて、案内筒14内に上
昇流が形成されて槽内液は案内筒14−ドラフト
管15の吐出口17−材16−案内筒14を強
制循環されると共に曝気処理が施され、その混合
液は開口10から沈殿室6に順次に移動されてゆ
き、沈殿室6で沈殿処理を受け汚泥は接触曝気室
5に重力返送され、他方、上澄液は流出管から放
流される。
The wastewater to be treated flows into the separation chamber 4 from the inflow pipe 7, undergoes precipitation and separation, and then flows into the contact aeration chamber 5 from the advection pipe 9. In this contact aeration chamber 5,
Due to the rotation of the impeller 13, an upward flow is formed in the guide tube 14, and the liquid in the tank is forcibly circulated through the guide tube 14, the discharge port 17 of the draft pipe 15, the material 16, and the guide tube 14, and is also subjected to aeration treatment. The mixed liquid is sequentially transferred from the opening 10 to the settling chamber 6, where the sludge undergoes sedimentation treatment and is returned to the contact aeration chamber 5 by gravity, while the supernatant liquid is discharged from the outflow pipe. be done.

この際、ドラフト管15の吐出口17の方向を
移流管9の移流口9aに対して回転調整して、第
3図、第4図に示すように、移流管9を介して接
触曝気室5内のSS等を含む混合液を分離室4に
返送しまたはそれを中止したり、さらには移流口
9aに対する吐出口17の方向をずらし、返送量
の調節を行うことができる。なお、曝気装置はイ
ンペラにかえて、案内筒内で散気を行うようにし
てもよい。
At this time, the direction of the discharge port 17 of the draft pipe 15 is rotationally adjusted with respect to the advection port 9a of the advection pipe 9, and as shown in FIGS. It is possible to return the mixed liquid containing SS and the like therein to the separation chamber 4 or to stop it, and furthermore to shift the direction of the discharge port 17 with respect to the advection port 9a to adjust the amount of return. Note that the aeration device may be replaced with an impeller and may be configured to diffuse air within the guide cylinder.

以上、この考案によれば、曝気装置の吐出口を
分離室の移流口との対向位置に回動調整しておく
ことにより、接触曝気室内の固形物を含む混合液
を前段の分離室に返送することができ、これによ
り、上記分離室内に流入して沈澱分離された固形
物を含まない液のみを上記接触曝気室内に流入さ
せることが可能となり、その繰り返しによつて、
上記接触曝気室内での浮遊固形物を大幅に減少さ
せることができて安定した効率的な汚水処理が行
える。また、上記曝気装置の吐出口の回動調整に
よつて、混合液の移送量および接触曝気室内の汚
泥濃度の調整を容易に行うことができる。
As described above, according to this invention, by rotating and adjusting the discharge port of the aeration device to a position opposite to the advection port of the separation chamber, the mixed liquid containing solids in the contact aeration chamber is returned to the preceding separation chamber. As a result, only the liquid that does not contain solids that has flowed into the separation chamber and has been precipitated and separated can flow into the contact aeration chamber, and by repeating this,
Suspended solids in the contact aeration chamber can be significantly reduced, allowing stable and efficient wastewater treatment. Further, by adjusting the rotation of the discharge port of the aeration device, the amount of mixed liquid transferred and the sludge concentration in the contact aeration chamber can be easily adjusted.

【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の縦断面図、第2
図はこの考案の要部の拡大縦断面図、第3図、第
4図は同要部の正面図を示す。 1……浄化槽本体、4……分離室、5……接触
曝気室、7……流入管、8……流出管、9……移
流管、14……案内筒、15……ドラフト管、1
7……吐出口。
Figure 1 is a longitudinal sectional view of one embodiment of this invention;
The figure shows an enlarged vertical sectional view of the main part of this invention, and FIGS. 3 and 4 show front views of the main part. 1... Septic tank body, 4... Separation chamber, 5... Contact aeration chamber, 7... Inflow pipe, 8... Outflow pipe, 9... Advection pipe, 14... Guide tube, 15... Draft pipe, 1
7...Discharge port.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 浄化槽本体内に設けられ、流入汚水の沈澱分離
を行う前段の分離室と、この分離室に移流口を介
して接続された接触曝気室と、該接触曝気室内に
設けられた案内筒と、この案内筒内の液体を揚上
させ放射方向に吐出させて槽内の液体を循環させ
る曝気装置とを備え、この曝気装置の吐出口を上
記移流口との対応位置で上記案内筒の上方に回転
可能に設け、上記接触曝気室内の固形物を含む混
合液を上記分離室内に返送可能にした浄化槽。
A pre-separation chamber provided in the septic tank main body for sedimentation and separation of inflow sewage, a contact aeration chamber connected to this separation chamber via an advection port, a guide tube provided in the contact aeration chamber, and an aeration device that circulates the liquid in the tank by lifting up the liquid in the guide tube and discharging it in a radial direction, and rotating the discharge port of the aeration device above the guide tube at a position corresponding to the advection port. The septic tank is configured such that the liquid mixture containing solids in the contact aeration chamber can be returned to the separation chamber.
JP1982029194U 1982-03-02 1982-03-02 septic tank Granted JPS58132593U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1982029194U JPS58132593U (en) 1982-03-02 1982-03-02 septic tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1982029194U JPS58132593U (en) 1982-03-02 1982-03-02 septic tank

Publications (2)

Publication Number Publication Date
JPS58132593U JPS58132593U (en) 1983-09-07
JPS6221354Y2 true JPS6221354Y2 (en) 1987-05-29

Family

ID=30041002

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1982029194U Granted JPS58132593U (en) 1982-03-02 1982-03-02 septic tank

Country Status (1)

Country Link
JP (1) JPS58132593U (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5532138U (en) * 1978-08-23 1980-03-01

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5532138U (en) * 1978-08-23 1980-03-01

Also Published As

Publication number Publication date
JPS58132593U (en) 1983-09-07

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