JPH0737758Y2 - Sewage septic tank - Google Patents

Sewage septic tank

Info

Publication number
JPH0737758Y2
JPH0737758Y2 JP14752489U JP14752489U JPH0737758Y2 JP H0737758 Y2 JPH0737758 Y2 JP H0737758Y2 JP 14752489 U JP14752489 U JP 14752489U JP 14752489 U JP14752489 U JP 14752489U JP H0737758 Y2 JPH0737758 Y2 JP H0737758Y2
Authority
JP
Japan
Prior art keywords
tank
treatment
treatment tank
air
sewage
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
JP14752489U
Other languages
Japanese (ja)
Other versions
JPH0386096U (en
Inventor
八郎 佐藤
丈衛 佐藤
良人 北井
大 原田
和之 本田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kubota Corp
Original Assignee
Kubota Corp
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 Kubota Corp filed Critical Kubota Corp
Priority to JP14752489U priority Critical patent/JPH0737758Y2/en
Publication of JPH0386096U publication Critical patent/JPH0386096U/ja
Application granted granted Critical
Publication of JPH0737758Y2 publication Critical patent/JPH0737758Y2/en
Anticipated expiration legal-status Critical
Expired - Lifetime 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)
  • Biological Treatment Of Waste Water (AREA)

Description

【考案の詳細な説明】 〔産業上の利用分野〕 この考案は汚水浄化槽に関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial field of application] The present invention relates to a sewage purification tank.

〔従来の技術〕 従来、家庭の屎尿及び雑排水の浄化槽として、嫌気性処
理槽、好気性処理槽、沈澱槽及び消毒層槽を備え、順次
汚水を移流させつつ浄化処理していく小型合併浄化槽等
の汚水浄化槽が広く知られている。
[Prior art] Conventionally, as a septic tank for domestic human waste and gray water, a small combined septic tank that has an anaerobic treatment tank, an aerobic treatment tank, a sedimentation tank, and a disinfection layer tank, and performs purification treatment while sequentially advancing sewage. Sewage septic tanks such as are widely known.

上記での処理汚水はBDD値20mg/l以下とされるが一般にB
DD値10mg/l以下を維持することは困難であり、また硝化
は必ずしも充分でない問題があった。
Although the treated sewage treated above has a BDD value of 20 mg / l or less, it is generally B
It was difficult to maintain a DD value of 10 mg / l or less, and nitrification was not always sufficient.

そこで、汚水の高度処理を目的として、上記した汚水浄
化槽にさらに三次処理槽を接続し、この三次処理槽でば
っ気処理を行い有機物の高度処理を行うと共に硝化を促
進しアンモニアを除去する手段が提案され且つ実施され
ている。
Therefore, for the purpose of advanced treatment of sewage, a method is proposed in which a tertiary treatment tank is further connected to the above-mentioned sewage purification tank, aeration treatment is performed in this tertiary treatment tank to perform advanced treatment of organic substances, and nitrification is promoted to remove ammonia. Has been and is being implemented.

〔従来技術の問題点〕[Problems of conventional technology]

しかしながら、前述の三次処理槽によるばっ気処理によ
る場合は、好気性処理時に汚水の硝化が促進するもの
の、泥水のPHが下がりすぎることがあり、さらに、処理
汚水の低負荷高酸素条件によりミジンコが大量発生し、
これらが浄化処理に必要な生物膜を食い荒らし剥離汚泥
を増加させたり、処理能力の低下を招く欠点があった。
However, in the case of aeration treatment by the above-mentioned tertiary treatment tank, although nitrification of wastewater is promoted during aerobic treatment, PH of mud may be too low. Occur in large numbers,
These have the drawbacks of eating up the biofilm necessary for purification treatment, increasing the amount of peeled sludge, and lowering the treatment capacity.

〔考案が解決しようとする課題〕[Problems to be solved by the device]

この考案は上記問題点に鑑み、汚水浄化槽に三次処理槽
を設けた場合において、排出水のPHを充分に平準化さ
せ、かつミジンコの発生を抑制できる汚水浄化槽を提供
することを目的としてなされたものである。
In view of the above problems, the present invention has been made for the purpose of providing a sewage purification tank capable of sufficiently leveling the PH of discharged water and suppressing the generation of Daphnia when the sewage purification tank is provided with a tertiary treatment tank. It is a thing.

〔課題を解決する技術〕[Technology for solving problems]

即ち、この考案の汚水浄化槽は、嫌気性処理槽、好気性
処理槽、沈澱槽及び消毒槽を備え、順次汚水を移流させ
つつ浄化処理していく汚水浄化槽において、該汚水浄化
槽より排出される処理水をさらに浄化処理する三次処理
槽が前記汚水浄化槽に接続され、該三次処理槽には前記
好気性処理槽とは別に設けたブロアより給気される散気
管が設けられていると共に、該ブロアより前記散気管に
給気する空気供給管が分岐され、該分岐管にはタイマー
により間歇作動される電磁弁を介して大気泡発生用散気
管が設けられて成ることを特徴とするものである。
That is, the sewage purification tank of the present invention comprises an anaerobic treatment tank, an aerobic treatment tank, a settling tank and a disinfection tank, and in the sewage purification tank that purifies while sequentially advancing sewage, the treatment discharged from the sewage purification tank A tertiary treatment tank for further purifying water is connected to the sewage treatment tank, and the tertiary treatment tank is provided with an air diffuser for supplying air from a blower provided separately from the aerobic treatment tank. The air supply pipe for supplying air to the air diffuser is branched from the air diffuser, and a large bubble generating air diffuser is provided in the branched pipe via an electromagnetic valve that is intermittently operated by a timer. ..

〔実施例〕〔Example〕

次に、この考案の実施例を説明する。 Next, an embodiment of this invention will be described.

第1図はこの考案の実施例の断面図、第2図(イ)及び
(ロ)はこの考案の実施例の電磁弁作動状態を示すグラ
フである。
FIG. 1 is a sectional view of an embodiment of the present invention, and FIGS. 2 (a) and 2 (b) are graphs showing an operating state of a solenoid valve of the embodiment of the present invention.

この考案の汚水浄化槽1は、嫌気性処理槽2A、2B、好気
性処理槽3、沈殿槽4及び消毒槽5を備え、順次汚水を
移流させつつ浄化処理していく汚水浄化槽1′におい
て、汚水浄化槽より排出される処理水をさらに浄化処理
する三次処理槽6が汚水浄化槽1′に接続され、三次処
理槽6には好気性処理槽3とは別に設けたブロア8より
給気される散気管7が設けられていると共に、このブロ
ア8より散気管7に給気する空気供給管8Bが分岐され、
該分岐管にはタイマー8Aにより間歇作動される電磁弁9
を介して大気泡発生用散気管10が設けられて構成されて
いる。
The sewage purification tank 1 of this invention comprises anaerobic treatment tanks 2A and 2B, an aerobic treatment tank 3, a settling tank 4 and a disinfection tank 5, and in the sewage purification tank 1'which performs purification treatment while sequentially advancing sewage, A tertiary treatment tank 6 for further purifying the treated water discharged from the septic tank is connected to the sewage purification tank 1 ', and the tertiary treatment tank 6 is supplied with an air diffuser from a blower 8 provided separately from the aerobic treatment tank 3. 7 is provided, and the air supply pipe 8B for supplying air to the diffuser pipe 7 is branched from this blower 8,
A solenoid valve 9 is intermittently operated by a timer 8A on the branch pipe.
An air diffuser 10 for generating large bubbles is provided via the above.

第1図において3Aは好気性処理槽3内に設けられた散気
管、3Bは散気管3Aに送気するブロアを示す。
In FIG. 1, 3A indicates an air diffuser provided in the aerobic treatment tank 3, and 3B indicates a blower for supplying air to the air diffuser 3A.

上記において、電磁弁9に対する間歇制御は、第2図
(イ)に示すように数時間サイクルでON、OFFを繰り返
す制御の他、第2図(ロ)に示すように、OFFの時間中
に短い時間だけONを間歇作動させる制御が行われる。
In the above, the intermittent control for the solenoid valve 9 is such that, as shown in FIG. 2 (a), ON / OFF is repeated in a cycle of several hours, and as shown in FIG. 2 (B), during the OFF time. The control that intermittently activates ON is performed for a short time.

これらは汚水の性質、量、流入パターン及び気候的条件
等を勘案して適宜選定される。
These are appropriately selected in consideration of the nature, quantity, inflow pattern, climatic conditions, etc. of sewage.

〔作用〕[Action]

この考案において、汚水浄化槽1′より排出された汚水
は三次処理槽6でさらに浄化処理されるが、この場合、
汚水中に高率の散気と大気泡散気とが間歇的に行われる
ため、高率散気時は供給酸素量が十分となりBODの除去
が行われると共に硝化が進む。一方大気泡散気時は汚水
中に溶存可能な酸素供給量が少なく、主に大気泡上昇に
より生じる循環流により汚水と生物膜との高率的な接触
が図られ、低酸素供給量より過度の硝化によるPH低下が
抑制されると共にミジンコの発生も抑制される。
In this invention, the sewage discharged from the sewage purification tank 1'is further purified by the tertiary treatment tank 6. In this case,
Since high-rate aeration and large-bubble aeration are intermittently performed in the wastewater, the amount of oxygen supplied is sufficient at the time of high-rate aeration, BOD is removed, and nitrification proceeds. On the other hand, when large air bubbles are diffused, the amount of oxygen that can be dissolved in the wastewater is small, and the circulation flow generated by the rise of the large bubbles enables highly efficient contact between the wastewater and the biofilm, which is more than the low oxygen supply amount. The decrease in PH due to nitrification of erythrocyte is suppressed and the generation of Daphnia magna is also suppressed.

従って三次処理により、例えば処理水BOD値10ppm以下を
維持できるなど、十分な汚水処理が行われるものであ
る。
Therefore, by the tertiary treatment, for example, the treated water BOD value can be maintained at 10 ppm or less, and sufficient sewage treatment is performed.

さらに、第2図(ロ)に示すように、OFFの時間中に短
い時間だけONを間歇作動した場合は、微細散気気泡によ
り処理水が攪拌されるので、処理液と微生物との接触効
率が向上され、より均一な処理が可能となる。
Further, as shown in Fig. 2 (b), when the ON is intermittently operated for a short time during the OFF time, the treated water is agitated by the fine air bubbles, so that the contact efficiency between the treatment liquid and the microorganism is high. Is improved and a more uniform treatment is possible.

また、前置処理装置において接触ばっ気槽の液を第1室
常時返送循環するエアリフトポンプ11を設置した場合
は、さらに安定した処理が可能になる。
Further, in the pretreatment device, when the air lift pump 11 which constantly circulates the liquid in the contact aeration tank is constantly returned and circulated, more stable treatment becomes possible.

〔効果〕〔effect〕

この考案は以上説明したように、三次処理槽における2
種類の散気によって従来に比し、BOD値の低い、またPH
の平準化された安定処理水とすることができるのであ
る。
As described above, this invention has two features in the tertiary treatment tank.
Lower BOD value and PH than before due to different types of aeration
It is possible to obtain a leveled and stabilized treated water.

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

第1図はこの考案の実施例の断面図、第2図(イ)及び
(ロ)は実施例の間歇散気の状態を示すグラフである。
FIG. 1 is a cross-sectional view of an embodiment of the present invention, and FIGS. 2 (a) and 2 (b) are graphs showing an intermittent aeration state of the embodiment.

───────────────────────────────────────────────────── 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 久保 田鉄工株式会社滋賀工場内 (72)考案者 本田 和之 滋賀県甲賀郡甲西町高松2番地の1 久保 田鉄工株式会社滋賀工場内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Dai Harada, 1 of 2 Takamatsu, Kosai-cho, Koga-gun, Shiga Prefecture Kubo Tatekko Co., Ltd. Shiga Factory (72) Kazuyuki Honda, Takamatsu, Kosai-cho, Koga-gun, Shiga Prefecture No.1 Kubo Tetsuko Co., Ltd. Shiga Factory

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】嫌気性処理槽、好気性処理槽、沈澱槽及び
消毒槽を備え、順次汚水を移流させつつ浄化処理してい
く汚水浄化槽において、該汚水浄化槽より排出される処
理水をさらに浄化処理する三次処理槽が前記汚水浄化槽
に接続され、該三次処理槽には前記好気性処理槽とは別
に設けたブロアより給気される散気管が設けられている
と共に、該ブロアより前記散気管に給気する空気供給管
が分岐され、該分岐管にはタイマーにより間歇作動され
る電磁弁を介して大気泡発生用散気管が設けられて成る
ことを特徴とする汚水浄化槽。
1. A sewage purification tank comprising an anaerobic treatment tank, an aerobic treatment tank, a settling tank and a disinfection tank, which successively purifies the wastewater while advancing it, and further purifies the treated water discharged from the wastewater purification tank. A tertiary treatment tank for treatment is connected to the wastewater purification tank, and an air diffuser for supplying air from a blower provided separately from the aerobic treatment tank is provided in the tertiary treatment tank, and the diffuser pipe is provided from the blower. A sewage purification tank characterized in that an air supply pipe for supplying air is branched, and an air diffusion pipe for generating large bubbles is provided in the branched pipe via an electromagnetic valve intermittently operated by a timer.
JP14752489U 1989-12-20 1989-12-20 Sewage septic tank Expired - Lifetime JPH0737758Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14752489U JPH0737758Y2 (en) 1989-12-20 1989-12-20 Sewage septic tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14752489U JPH0737758Y2 (en) 1989-12-20 1989-12-20 Sewage septic tank

Publications (2)

Publication Number Publication Date
JPH0386096U JPH0386096U (en) 1991-08-30
JPH0737758Y2 true JPH0737758Y2 (en) 1995-08-30

Family

ID=31694032

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14752489U Expired - Lifetime JPH0737758Y2 (en) 1989-12-20 1989-12-20 Sewage septic tank

Country Status (1)

Country Link
JP (1) JPH0737758Y2 (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS547050B2 (en) * 1973-01-20 1979-04-03

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS547050U (en) * 1977-06-16 1979-01-18

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS547050B2 (en) * 1973-01-20 1979-04-03

Also Published As

Publication number Publication date
JPH0386096U (en) 1991-08-30

Similar Documents

Publication Publication Date Title
KR100422211B1 (en) Management Unit and Method of Foul and Waste Water
KR20160147560A (en) Nitrogen and phosphorus removal device for wastewater
KR100527172B1 (en) A method and apparatus for nitrogenous waste water of nitrogen and sewage
JPH1034185A (en) Drainage treatment method
JPH0737758Y2 (en) Sewage septic tank
JPH05337492A (en) Biological treatment of sewage
JP2912905B1 (en) Denitrification and dephosphorization of organic wastewater
KR100321680B1 (en) Advance wastewater treatment method by wastewater passage alternation
KR100375413B1 (en) Removal Methods of Nitrogen and phosphorus in wastewater using external carbon source
KR100438323B1 (en) High intergated Biological Nutrient Removal System
KR100513567B1 (en) Wastewater Purification Apparatus
CN206985984U (en) A kind of system of deeply treating wastewater
KR100530555B1 (en) Small-scale facility and method for treating wastewater biologically
KR100462578B1 (en) The purification method of an organic waste water with high density
JPH0717437Y2 (en) Sewage septic tank
KR100478010B1 (en) A waste water disposal plant
KR960011888B1 (en) Method and apparatus for biological treatment of waste water including nitrogen and phosphorus
JPH05138186A (en) Treatment of drainage discharged from purification tank
JPS6222678B2 (en)
JP3919455B2 (en) Advanced denitrification method for waste water
JPH04110198U (en) Anaerobic/aerobic activated sludge treatment equipment
KR100318367B1 (en) Waste water treatment apparatus
KR950000212B1 (en) Waste water clarifier
KR19990030405A (en) Wastewater Purification Using Distribution Inflow
JPH07136678A (en) Wastewater treatment method and tank