JPS5817674Y2 - septic tank - Google Patents

septic tank

Info

Publication number
JPS5817674Y2
JPS5817674Y2 JP1979092932U JP9293279U JPS5817674Y2 JP S5817674 Y2 JPS5817674 Y2 JP S5817674Y2 JP 1979092932 U JP1979092932 U JP 1979092932U JP 9293279 U JP9293279 U JP 9293279U JP S5817674 Y2 JPS5817674 Y2 JP S5817674Y2
Authority
JP
Japan
Prior art keywords
chamber
separation chamber
nitrification
liquid
septic tank
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
JP1979092932U
Other languages
Japanese (ja)
Other versions
JPS5610994U (en
Inventor
早川登
Original Assignee
株式会社 西原環境衛生研究所
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 株式会社 西原環境衛生研究所 filed Critical 株式会社 西原環境衛生研究所
Priority to JP1979092932U priority Critical patent/JPS5817674Y2/en
Publication of JPS5610994U publication Critical patent/JPS5610994U/ja
Application granted granted Critical
Publication of JPS5817674Y2 publication Critical patent/JPS5817674Y2/en
Expired 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

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

Description

【考案の詳細な説明】 この考案は、硝化液の返送機能を有する浄化槽に関する
ものである。
[Detailed description of the invention] This invention relates to a septic tank having a function of returning nitrified liquid.

従来、例えば家庭用合併処理浄化槽等の流入汚水の流量
変動が激しい浄化槽は、第1図のように構成されていた
Conventionally, a septic tank, such as a household combined treatment septic tank, in which the flow rate of inflowing sewage fluctuates drastically, has been constructed as shown in FIG.

1は、分離室であり、この分離室1に流入した流入水は
その内の固形物が沈殿分離される。
Reference numeral 1 denotes a separation chamber, and the solids contained in the water flowing into the separation chamber 1 are precipitated and separated.

分離室1の分離液は、流量調整装置2を介して一定量ず
つ曝気室3に供給される。
The separated liquid in the separation chamber 1 is supplied in fixed amounts to the aeration chamber 3 via the flow rate adjustment device 2.

流量調整装置2は所定のスペースを有する流量調整室内
に設けられている。
The flow rate adjustment device 2 is provided in a flow rate adjustment chamber having a predetermined space.

この流量調整装置2は、上記分離室1への流入水量が変
動しても曝気室3への供給量を変動させないために設け
られる。
This flow rate adjustment device 2 is provided to prevent the amount of water supplied to the aeration chamber 3 from changing even if the amount of water flowing into the separation chamber 1 changes.

特に家庭用のものでは流量変動のピークが太きい。Especially for household use, the peak of flow rate fluctuation is large.

接触F材の充てんされた曝気室3で曝気された曝気水は
、同じく接触炉材の充てんされた硝化室4に供給されて
硝酸化されろ。
The aerated water aerated in the aeration chamber 3 filled with contact F material is supplied to the nitrification chamber 4 also filled with contact furnace material and nitrified.

なお、この場合、曝気室3と硝化室4は仕切らず一室と
してもよい。
In addition, in this case, the aeration chamber 3 and the nitrification chamber 4 may be one room without being partitioned.

また、曝気室3の後にSS(浮遊固形物)捕捉用の汚泥
貯留室を設け、これを通してから硝化室4に移流させて
もよい。
Further, a sludge storage chamber for capturing SS (suspended solids) may be provided after the aeration chamber 3, and the sludge may be advected to the nitrification chamber 4 after passing through this.

そして、硝化室4で硝化された処理水は消毒室5で消毒
された後に放流される。
The treated water nitrified in the nitrification chamber 4 is disinfected in a disinfection chamber 5 and then discharged.

この考案は、以上の浄化槽において脱窒機能を付与する
ためになされたもので、流量調整装置により分離室と硝
化室(曝気室)との間に生じる落差を利用して硝化室の
硝化液を嫌気的条件下の分離室に返送することによって
、脱窒菌の作用により硝化液を容易に脱窒することがで
きる浄化槽を提供することを目的とするものである。
This idea was devised to provide a denitrification function to the above-mentioned septic tank, and the nitrified liquid in the nitrification chamber is reduced by using the head created between the separation chamber and the nitrification chamber (aeration chamber) by the flow rate adjustment device. The object of the present invention is to provide a septic tank that can easily denitrify nitrified liquid by the action of denitrifying bacteria by returning it to a separation chamber under anaerobic conditions.

以下、この考案の一実施例を第2図〜第4図を参照して
詳細に説明する。
Hereinafter, one embodiment of this invention will be described in detail with reference to FIGS. 2 to 4.

先ず第2図は、分離室1の流入水量の変動と硝化室(曝
気室)水量との関係を示すものである。
First, FIG. 2 shows the relationship between fluctuations in the amount of water flowing into the separation chamber 1 and the amount of water in the nitrification chamber (aeration chamber).

例えば、今分離室1への流入水量が増加すると。For example, if the amount of water flowing into the separation chamber 1 increases now.

液位はLWLからHWLに上昇して前述のように流量調
整装置を介して曝気室3に一定量の分離液が供給される
The liquid level rises from LWL to HWL, and a fixed amount of separated liquid is supplied to the aeration chamber 3 via the flow rate adjustment device as described above.

このように、分離室1と曝気室3(硝化室4)との間に
は、流量調整装置があるために液位に落差を生じる。
In this way, since there is a flow rate adjustment device between the separation chamber 1 and the aeration chamber 3 (nitrification chamber 4), a drop occurs in the liquid level.

第3図は、上記の落差を利用して硝化室4の硝化液を第
1図矢印aのように分離室1側に返送するようにしたこ
の考案の第1の実施例である。
FIG. 3 shows a first embodiment of this invention in which the nitrified liquid in the nitrification chamber 4 is returned to the separation chamber 1 side as indicated by the arrow a in FIG. 1 by utilizing the above-mentioned head.

6は、硝化液移流管で、例えば第1図のbの部分に設け
られている。
Reference numeral 6 denotes a nitrification liquid advection tube, which is provided, for example, at the portion b in FIG.

移流管6の下部には、内部にフロート(一方向流通弁)
8を有するパイプ1が直結されており、連結部9は径小
にしぼられている。
At the bottom of the advection pipe 6, there is a float (one-way flow valve) inside.
8 are directly connected to each other, and the connecting portion 9 is reduced in diameter.

従って、今分離室1内の液位が、ビータHWLIか又は
基準位HWL2以上の場合には、フロート8は連結部9
の部分に上昇してパイプ1内を閉塞している。
Therefore, if the liquid level in the separation chamber 1 is now higher than the beater HWLI or the reference level HWL2, the float 8 is moved to the connecting portion 9.
It rises to the part shown in FIG. 1 and blocks the inside of the pipe 1.

そのために硝化室4よりの硝化液は分離室1内には返送
されない。
Therefore, the nitrified liquid from the nitrification chamber 4 is not returned to the separation chamber 1.

ところが、分離室1側の液位が、最低位LWLまで低下
すると、基準位LWL2より低下した時点でフロート8
がパイプ1内を開放し硝化室4の硝化液が分離室1内に
流入し始め、LWLの時点で最大となる。
However, when the liquid level on the separation chamber 1 side drops to the lowest level LWL, the float 8
opens the inside of the pipe 1, and the nitrified liquid in the nitrification chamber 4 begins to flow into the separation chamber 1, reaching a maximum at LWL.

このようにして、硝化液は分離室1内に返送され、自動
的に脱窒される。
In this way, the nitrifying liquid is returned into the separation chamber 1 and automatically denitrified.

パイプγは厳密な意味でのパイプである必要はなく、フ
ロート8を支持できればなんでもよい。
The pipe γ does not need to be a pipe in the strict sense, and may be anything that can support the float 8.

また、第4図は、この考案の第2の実施例であり、移流
部を移流管構成ではなく、水圧差によって開閉する逆毛
弁構成としたものである。
Further, FIG. 4 shows a second embodiment of this invention, in which the advection section is not configured as an advection tube, but is configured as a back-flow valve that opens and closes depending on the water pressure difference.

10は、硝化液を移流するための連通孔で、その分離室
1端には弁板(一方向流通弁)11が上部で軸着されて
いる。
Reference numeral 10 denotes a communication hole for advection of the nitrification liquid, and a valve plate (one-way flow valve) 11 is pivoted at the upper part of one end of the separation chamber.

従って、今分離室1内の液位W1が硝化室4の液位W2
よりも高いか又は同位の場合には、弁板(一方向流通弁
)11は図示のように閉塞していて硝化液の移流は起ら
ない。
Therefore, the liquid level W1 in the separation chamber 1 is now the liquid level W2 in the nitrification chamber 4.
If it is higher than or at the same level, the valve plate (one-way flow valve) 11 is closed as shown in the figure, and advection of the nitrifying liquid does not occur.

ところが、WlがW2よりも低下すると、硝化室4内の
水圧が分離室1側よりも高くなって弁板(一方向流通弁
)11は矢印方向に開放され、硝化液は分離室1側に移
流する。
However, when Wl becomes lower than W2, the water pressure in the nitrification chamber 4 becomes higher than that on the separation chamber 1 side, and the valve plate (one-way flow valve) 11 opens in the direction of the arrow, and the nitrification liquid flows toward the separation chamber 1 side. Advect.

この図の場合、弁板(一方向流通弁)11は自重により
、連通孔10におさえつげられているので水圧が一定値
以上になった時にのみ開放される。
In the case of this figure, the valve plate (one-way flow valve) 11 is held in the communication hole 10 by its own weight, so it is opened only when the water pressure exceeds a certain value.

硝化液の落差による移流方法は、上記実施例に限定され
ることはなく、ポールタンプ弁などを適宜採用すればよ
い。
The advection method using the head difference of the nitrifying liquid is not limited to the above embodiment, and a pole tump valve or the like may be adopted as appropriate.

なお、以上の説明では、家庭用合併処理浄化槽を例とし
て説明したが、この考案は、他の全ての浄化槽にも適用
することができることは言うまでもない。
In addition, in the above explanation, the household combined treatment septic tank was explained as an example, but it goes without saying that this invention can be applied to all other septic tanks.

以上のようにこの考案によれば、流量調整装置によって
生じる水位落差を利用して硝化液を分離室に返送するよ
うにしたので、自動的かつ容易に簡単な構成で脱窒機能
を実現することができる。
As described above, according to this invention, the nitrifying liquid is returned to the separation chamber by using the water level drop generated by the flow rate adjustment device, so the denitrification function can be automatically and easily realized with a simple configuration. I can do it.

また、曝気室、硝化室を沖材を充てんした接触曝気室と
すれば、硝化液を返送しても曝気室、硝化室内に活性汚
泥を保持できる。
Furthermore, if the aeration chamber and nitrification chamber are made into contact aeration chambers filled with offshore wood, activated sludge can be retained in the aeration chamber and nitrification chamber even if the nitrification solution is returned.

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

第1図は、従来の浄化槽の平面図、第2図は、浄化槽の
液位状態を説明するための断面図、第3図は、この考案
の第1の実施例による浄化槽の要部の側面図、第4図は
、同第2の実施例による浄化槽の要部の断面図である。 1・・・・・・分離室、2・・・・・・流量調整装置、
3・・・・・曝気室、4・・・・・・硝化室、6・・・
・崎肖化液移流管、8・・・・・・フロート(一方向流
通弁)、10・・・・・・連通孔、11・・・・・青板
(一方向流通弁)・
Fig. 1 is a plan view of a conventional septic tank, Fig. 2 is a sectional view for explaining the liquid level state of the septic tank, and Fig. 3 is a side view of the main parts of a septic tank according to the first embodiment of this invention. 4 are sectional views of the main parts of the septic tank according to the second embodiment. 1...Separation chamber, 2...Flow rate adjustment device,
3...Aeration chamber, 4...Nitrification chamber, 6...
・Sakishoka liquid advection pipe, 8...Float (one-way flow valve), 10...Communication hole, 11... Blue plate (one-way flow valve)・

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 流入汚水中の固形物を分離する分離室と、この分離室の
分離液が流量調整装置を介してぜ定量ずつ供給される曝
気室と、この曝気室と上記分離室との連通路に設けられ
、該曝気室内の液位が該分離室の液位より高くなった時
にのみ開(一方向流通弁とを備えた浄化槽。
A separation chamber that separates solids in inflowing wastewater, an aeration chamber to which the separated liquid of this separation chamber is supplied in fixed amounts via a flow rate adjustment device, and a communication path between this aeration chamber and the separation chamber are provided. , a septic tank equipped with a one-way flow valve that opens only when the liquid level in the aeration chamber becomes higher than the liquid level in the separation chamber.
JP1979092932U 1979-07-04 1979-07-04 septic tank Expired JPS5817674Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1979092932U JPS5817674Y2 (en) 1979-07-04 1979-07-04 septic tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1979092932U JPS5817674Y2 (en) 1979-07-04 1979-07-04 septic tank

Publications (2)

Publication Number Publication Date
JPS5610994U JPS5610994U (en) 1981-01-30
JPS5817674Y2 true JPS5817674Y2 (en) 1983-04-09

Family

ID=29325881

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1979092932U Expired JPS5817674Y2 (en) 1979-07-04 1979-07-04 septic tank

Country Status (1)

Country Link
JP (1) JPS5817674Y2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6293531U (en) * 1985-11-29 1987-06-15
JPH0725280Y2 (en) * 1989-10-17 1995-06-07 株式会社クボタ Sewage treatment equipment
JPH0824918B2 (en) * 1991-07-06 1996-03-13 日本碍子株式会社 Aeration tank for anaerobic / aerobic treatment and scum outflow method in this aeration tank

Also Published As

Publication number Publication date
JPS5610994U (en) 1981-01-30

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