JPH081036Y2 - Sewage septic tank - Google Patents

Sewage septic tank

Info

Publication number
JPH081036Y2
JPH081036Y2 JP1990062406U JP6240690U JPH081036Y2 JP H081036 Y2 JPH081036 Y2 JP H081036Y2 JP 1990062406 U JP1990062406 U JP 1990062406U JP 6240690 U JP6240690 U JP 6240690U JP H081036 Y2 JPH081036 Y2 JP H081036Y2
Authority
JP
Japan
Prior art keywords
tank
sewage
treatment tank
blower
contact aeration
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 - Fee Related
Application number
JP1990062406U
Other languages
Japanese (ja)
Other versions
JPH0422097U (en
Inventor
八郎 佐藤
広佳 中島
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 JP1990062406U priority Critical patent/JPH081036Y2/en
Publication of JPH0422097U publication Critical patent/JPH0422097U/ja
Application granted granted Critical
Publication of JPH081036Y2 publication Critical patent/JPH081036Y2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Jet Pumps And Other Pumps (AREA)
  • Treatment Of Biological Wastes In General (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し、詳しくは汚水浄化槽の
改良に関する。
[Detailed Description of the Invention] [Industrial field of application] The present invention relates to a sewage purification tank, and more particularly to an improvement of the sewage purification tank.

〔従来の技術〕[Conventional technology]

従来、家庭用の屎尿及び雑排水の汚水浄化槽として、
嫌気性微生物による一次処理槽、好気性微生物による二
次処理槽を有した合併浄化槽が公知である。
Conventionally, as a domestic wastewater and sewage purification tank for gray water,
A combined septic tank having a primary treatment tank with anaerobic microorganisms and a secondary treatment tank with aerobic microorganisms is known.

上記小型合併浄化槽においては排水汚水の脱窒を効果
的に行うため接触ばっ気槽より汚水の一部を嫌気処理槽
へ返送し汚水浄化槽内に循環経路を形成することがあ
る。
In the above-mentioned small combined septic tank, in order to effectively denitrify wastewater sewage, a part of the sewage may be returned from the contact aeration tank to the anaerobic treatment tank to form a circulation path in the sewage purification tank.

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

ところで、上記合併浄化槽では夜間には汚水の流入負
荷が殆ど無いので嫌気槽には脱窒用有機炭素源が乏しく
なり、折角汚水を循環しても十分な脱窒が行われない事
態に成りやすい。
By the way, since there is almost no inflow load of sewage in the combined septic tank at night, the anaerobic tank is scarce of the source of denitrifying organic carbon, and even if the sewage is circulated, sufficient denitrification is not likely to occur. .

従って、脱窒を効率良く行うには大略汚水の流入負荷
の多い昼間に循環式経路を形成する必要がある。また、
そのための制御装置としてタイマー、水位検出センサー
や電源等を組み合わせた制御装置を必要とし、装置が複
雑となる他、その保守点検も面倒となる問題もあった。
Therefore, in order to efficiently perform denitrification, it is necessary to form a circulation route during the daytime when the inflow load of sewage is large. Also,
As a control device for that purpose, a control device that combines a timer, a water level detection sensor, a power source, etc. is required, which complicates the device and also causes troublesome maintenance and inspection.

〔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、脱窒を効率良く行う汚
水循環経路の形成を、タイマーや電源などの複雑な制御
装置を用いることなく専ら昼間のみに限定ししかもその
ときの運転も非常に経済的に行え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 limits the formation of a sewage circulation path for efficient denitrification exclusively to the daytime without using a complicated control device such as a timer or a power supply, and the operation at that time is also very economical. The purpose of the present invention is to provide a sewage purification tank that can be used in various ways.

〔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処理槽、接触ばっ気
処理槽、沈殿槽および消毒槽を備えた合併浄化槽の前記
接触ばっ気処理槽より嫌気処理槽へ向け汚水返送管が設
けられ、該汚水返送管のエアリフトポンプの空気供給ブ
ロワが前記接触ばっ気処理槽へ散気を行う散気管用ブロ
ワとは別に設けられ、該エアリフトポンプの空気供給ブ
ロワは太陽電池を電源として蓄電池を介することなく直
接駆動されるよう構成したことを特徴とするものであ
る。
That is, the sewage purification tank of the present invention is provided with a sewage return pipe from the contact aeration treatment tank of the combined sewage treatment tank including an anaerobic treatment tank, a contact aeration treatment tank, a precipitation tank and a disinfection tank to the anaerobic treatment tank. The air supply blower of the pipe air lift pump is provided separately from the diffuser pipe blower that diffuses air to the contact aeration processing tank, and the air supply blower of the air lift pump is directly driven by the solar cell as a power source without using a storage battery. It is characterized by being configured as described above.

〔実施例〕〔Example〕

次にこの発明の実施例を説明する。 Next, an embodiment of the present invention will be described.

第1図はこの発明の実施例の断面図である。 FIG. 1 is a sectional view of an embodiment of the present invention.

この考案の汚水浄化槽1は、嫌気処理槽2、接触ばっ
気処理槽3、沈殿槽4及び消毒槽5を備え、汚水Wを順
次移流させつつ浄化処理していく合併浄化槽1におい
て、接触ばっ気処理槽3より嫌気処理槽2へ向け汚水返
送管3Aが設けられ、汚水返送管のエアリフトポンプ6の
空気供給ブロワ7が接触ばっ気処理槽3へ散気を行う散
気管用ブロワ8とは別に設けられ、エアリフトポンプの
空気供給ブロワ7は太陽電池9を電源として蓄電池を介
することなく直接駆動されるよう構成されている。
The sewage purification tank 1 of the present invention is provided with an anaerobic treatment tank 2, a contact aeration treatment tank 3, a settling tank 4 and a disinfection tank 5, and in the combined purification tank 1 in which sewage W is sequentially adsorbed and purified, contact aeration is performed. A sewage return pipe 3A is provided from the treatment tank 3 to the anaerobic treatment tank 2, and an air supply blower 7 of an air lift pump 6 of the sewage return pipe is in contact with the blower 8 for a diffuser pipe which diffuses air into the aeration treatment tank 3. The air supply blower 7 of the air lift pump is configured so as to be directly driven by using the solar cell 9 as a power source without using a storage battery.

〔作用〕[Action]

この考案の汚水浄化槽1において、汚水Wは前述の用
に各処理槽を移流しつつ浄化されていくが、接触ばっ気
槽内3の一部の汚水はエアリフトポンプ6により汚水返
送管3Aを介して嫌気処理槽2へと返送される。
In the sewage purification tank 1 of the present invention, the sewage W is purified while advancing through the respective treatment tanks as described above, but a part of the sewage in the contact aeration tank 3 is passed through the sewage return pipe 3A by the air lift pump 6. And returned to the anaerobic treatment tank 2.

この時のエアリフトポンプ6の駆動電源は蓄電池を介
することなく直接太陽電池9とされているので日中の明
るい時でなければ駆動せず、従って制御装置を設けるこ
となく昼間だけ選択的に循環経路を形成させることがで
きる。しかも、エアリフトポンプ6による返送水量は太
陽高度と比例したカーブを描くのでこのカーブに従って
日中のみ返送が行われる。又、循環水量は多少の変動が
許容されるので、太陽光の強弱によるブロワ能力の変動
も大きな問題とならない。
At this time, the drive power source of the air lift pump 6 is the solar cell 9 directly without passing through the storage battery, so it is not driven unless it is bright in the daytime. Therefore, the circulation route is selectively provided only during the daytime without providing a control device. Can be formed. Moreover, since the amount of water returned by the air lift pump 6 draws a curve proportional to the sun's altitude, the water is returned only during the day following this curve. Further, since the amount of circulating water is allowed to fluctuate somewhat, fluctuations in the blower capacity due to the intensity of sunlight are not a big problem.

〔効果〕〔effect〕

以上説明したように、この考案の汚水浄化槽は、脱窒
に必要な有機炭素源の多い日中に限り自動的に汚水を循
環させ、しかもその駆動電源は太陽電池を直接的な電源
としているため、商用電源を必要とせず、また昼間のみ
運転を行わせるためのタイマーなどの制御装置も必要と
せず選択的に汚水返送が行えるので非常に経済的な運転
が可能となる。また、エアリフトポンプ6による返送水
量は太陽高度と比例したカーブを描き、このカーブに従
って日中のみ返送が行われ、早朝と夜間の汚水供給のピ
ーク時には返送が停止されるため、早朝夜間のピーク時
にはSSの次槽への移流が防止され、前夜と朝の汚水供給
負荷に対して硝化反応が進んでから、日中に効率的に硝
化液を返送できる利点を有し、また一般に、好天の場合
洗濯をする確立が高く、洗濯排水流入後に返送水量が太
陽高度に比例して増加するため、硝化反応が十分進んだ
後に処理水を効率的に返送できて脱窒反応の促進にも適
する効果を有する。
As explained above, the wastewater septic tank of the present invention automatically circulates the wastewater only during the daytime when there are many organic carbon sources necessary for denitrification, and its drive power source uses a solar cell as a direct power source. In addition, it does not require a commercial power source and does not require a control device such as a timer for operating only in the daytime, and the sewage can be selectively returned, so that a very economical operation can be performed. In addition, the amount of water returned by the air lift pump 6 draws a curve proportional to the sun's altitude and is returned only during the day according to this curve, and the return is stopped at the peak of the dirty water supply in the early morning and at night, so at the peak of early morning and night. It has the advantage of being able to efficiently return the nitrification solution during the day after the SS is prevented from advancing to the next tank and the nitrification reaction progresses against the sewage supply load on the night before and in the morning. In this case, the probability of washing is high, and the amount of returned water increases in proportion to the sun's altitude after the inflow of laundry drainage, so that the treated water can be efficiently returned after the nitrification reaction has sufficiently progressed, and it is also suitable for promoting the denitrification reaction. Have.

また雨天時は前記と逆に返送水量が減少するが、同時
に洗濯等による負荷も少ないので問題はない。
On the other hand, in rainy weather, the amount of water to be returned decreases, but at the same time, there is no problem because the load due to washing and the like is small at the same time.

なお、汚水返送用エアリフトポンプは容量の小さいも
ので良いので電源の太陽電池の容量も小さく経済的であ
る。又、DCモータを用いれば直交変換装置も不要でコン
パクトなシステムとなる。
The airlift pump for returning sewage may have a small capacity, so that the capacity of the solar cell as a power source is small and economical. Also, if a DC motor is used, a quadrature converter is not required and the system becomes compact.

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

第1図はこの発明の実施例の断面図である。 FIG. 1 is a sectional view of an embodiment of the present invention.

───────────────────────────────────────────────────── 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 株式 会社クボタ滋賀工場内 (72)考案者 本田 和之 滋賀県甲賀郡甲西町高松2番地の1 株式 会社クボタ滋賀工場内 (56)参考文献 特開 平1−228593(JP,A) 高橋、浜川、後川編「太陽光発電」 (1980−2−20)森川出版P.455 ─────────────────────────────────────────────────── ─── Continuation of front page (72) Dai Harada, 2 Takamatsu, Kosai-cho, Koga-gun, Shiga Prefecture 1 Kubota Shiga factory (72) Creator Kazuyuki Honda 1 of 2 Takamatsu, Kosai-cho, Koga-gun, Shiga Prefecture Kubota Shiga Plant, Ltd. (56) References JP-A 1-228593 (JP, A) Takahashi, Hamakawa, Gogawa, "Solar Power" (1980-2-20) Morikawa Publishing P. 455

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】嫌気処理槽、接触ばっ気処理槽、沈殿槽お
よび消毒槽を備えた合併浄化槽の前記接触ばっ気処理槽
より嫌気処理槽へ向け汚水返送管が設けられ、該汚水返
送管のエアリフトポンプの空気供給ブロワが前記接触ば
っ気処理槽へ散気を行う散気管用ブロワとは別に設けら
れ、該エアリフトポンプの空気供給ブロワは太陽電池を
電源として蓄電池を介することなく直接駆動されるよう
構成したことを特徴とする汚水浄化槽。
1. A sewage return pipe is provided from the contact aeration treatment tank to the anaerobic treatment tank of the combined septic tank equipped with an anaerobic treatment tank, a contact aeration treatment tank, a precipitation tank and a disinfection tank, and The air supply blower of the air lift pump is provided separately from the air blower blower for diffusing to the contact aeration processing tank, and the air supply blower of the air lift pump is directly driven by the solar cell as a power source without using the storage battery. A sewage purification tank characterized by being configured as described above.
JP1990062406U 1990-06-13 1990-06-13 Sewage septic tank Expired - Fee Related JPH081036Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1990062406U JPH081036Y2 (en) 1990-06-13 1990-06-13 Sewage septic tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1990062406U JPH081036Y2 (en) 1990-06-13 1990-06-13 Sewage septic tank

Publications (2)

Publication Number Publication Date
JPH0422097U JPH0422097U (en) 1992-02-24
JPH081036Y2 true JPH081036Y2 (en) 1996-01-17

Family

ID=31591524

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1990062406U Expired - Fee Related JPH081036Y2 (en) 1990-06-13 1990-06-13 Sewage septic tank

Country Status (1)

Country Link
JP (1) JPH081036Y2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114656036A (en) * 2022-04-19 2022-06-24 陕西建工第十二建设集团有限公司 Rural sewage connects family well air stripping processing system based on photovoltaic system

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01228593A (en) * 1988-03-08 1989-09-12 Iseki Tory Tech Inc How to purify sewage

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
高橋、浜川、後川編「太陽光発電」(1980−2−20)森川出版P.455

Also Published As

Publication number Publication date
JPH0422097U (en) 1992-02-24

Similar Documents

Publication Publication Date Title
CN101525179B (en) A method for treating low-concentration ammonia-nitrogen wastewater by anaerobic ammonium oxidation
CN105110565A (en) Treatment method for slaughter wastewater
AU2008244181A1 (en) Method and equipment for processing waste water containing sulphides and ammonium
JP4527325B2 (en) Denitrification and methane fermentation equipment
JP3275351B2 (en) Anaerobic treatment of organic wastewater
JPH081036Y2 (en) Sewage septic tank
CN110240350A (en) It is a kind of to enhance sewerage integrated equipment and impact resistance method using nitrification liquid reflux
KR100304544B1 (en) Method for removing nitrogen and phosphorus using anaerobic digestion
JP3248233B2 (en) Activated sludge treatment method
CN107117710B (en) Enhanced biological phosphorus removal method
JPH0259000B2 (en)
CN105776750B (en) A kind of testing and measuring technology of the enzyme catalytic treatment landfill leachate of three-stage
JPH0698358B2 (en) Treatment method for human waste
CN205398228U (en) High ammonia -nitrogen concentration is low, and CN compares effluent disposal system
CN211546257U (en) Highly integrated improved A/A/O-MBR integrated sewage treatment device
KR100438323B1 (en) High intergated Biological Nutrient Removal System
CN114349290A (en) An enhanced phosphorus removal method based on MBBR sewage treatment process
JPH0975978A (en) Activated sludge treatment method and activated sludge treatment apparatus therefor
JPH08112600A (en) Combined septic tank
KR20010029666A (en) Removal Methods of Nitrogen and phosphorus in wastewater using external carbon source
KR20020094950A (en) Method and apparatus for wastewater treatments
KR950000212B1 (en) Wastewater Purification Method
TWI359794B (en)
JPS5976597A (en) Biological treatment of waste water containing nitrogen compound and dithionic acid
JP2693099B2 (en) Biological treatment method and acclimation method of microorganisms

Legal Events

Date Code Title Description
LAPS Cancellation because of no payment of annual fees