JPH05317872A - Septic tank - Google Patents

Septic tank

Info

Publication number
JPH05317872A
JPH05317872A JP25536692A JP25536692A JPH05317872A JP H05317872 A JPH05317872 A JP H05317872A JP 25536692 A JP25536692 A JP 25536692A JP 25536692 A JP25536692 A JP 25536692A JP H05317872 A JPH05317872 A JP H05317872A
Authority
JP
Japan
Prior art keywords
chamber
septic tank
treatment chamber
aerobic treatment
pipe
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.)
Withdrawn
Application number
JP25536692A
Other languages
Japanese (ja)
Inventor
Isao Miura
勲 三浦
Katsumi Nishimura
勝己 西村
Takamasa Tsuji
隆正 辻
Yoshinori Takezaki
義則 竹崎
Shuhei Kono
秀平 河野
Hirotoshi Oki
弘敏 沖
Takahiro Sakatani
孝宏 酒谷
Yoshihide Sekigami
佳秀 関上
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.)
AMUZU KK
Toto Ltd
Original Assignee
AMUZU KK
Toto Ltd
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 AMUZU KK, Toto Ltd filed Critical AMUZU KK
Priority to JP25536692A priority Critical patent/JPH05317872A/en
Publication of JPH05317872A publication Critical patent/JPH05317872A/en
Withdrawn legal-status Critical Current

Links

Abstract

PURPOSE:To suppress the load fluctuation of the septic tank to a lower level even if large solids are contained in sewage. CONSTITUTION:The body 1 of this septic tank is delineated, successively from an upstream side, by partition walls 2... to an anaerobic treatment chamber 3, an aerobic treatment chamber 4, a settling chamber 5 and a disinfecting chamber 6. The anaerobic treatment chamber 3 is further delineated with a preaeration chamber 8 by a partition wall 7. A sewage inflow pipe 9 from a toilet or kitchen faces this preaeration chamber 8 and a diffuser 10 for blowing the air to the bottom of the preaeration chamber 8 is provided. Further, a communicating port 11 with the anaerobic treatment chamber 3 is formed in the partition wall 7.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は便所や洗面所、風呂、厨
房などからの汚水を浄化して放流するための浄化槽に関
する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a septic tank for purifying and discharging sewage from a toilet, washroom, bath, kitchen or the like.

【0002】[0002]

【従来の技術】便所から排出されるし尿、洗面所、風
呂、厨房などから排出される雑排水等の浄化槽として、
1つの処理槽内を嫌気性処理室、好気性処理室、沈殿室
及び消毒室に仕切り、これらの室に順に汚水を通過させ
つつ浄化するようにした浄化槽が特開平2−22791
号公報等に開示され、また、嫌気性処理室及び好気性処
理室内に回転接触体を設け、有機物の低分子化を行うよ
うにした浄化槽が特公昭58−15038号公報に開示
されている。
2. Description of the Related Art As a septic tank for waste water discharged from toilets, toilets, baths, kitchens, etc.
JP-A-2-22791 discloses a septic tank in which one treatment tank is divided into an anaerobic treatment chamber, an aerobic treatment chamber, a precipitation chamber and a disinfection chamber, and these chambers are sequentially purified while passing sewage.
Japanese Patent Publication No. 58-15038 discloses a septic tank in which rotary contact bodies are provided in the anaerobic treatment chamber and the aerobic treatment chamber to lower the molecular weight of organic substances.

【0003】[0003]

【発明が解決しようとする課題】特開平2−22791
号公報等に開示されるように1つの処理槽を複数の室に
分け、各室で嫌気性処理および好気性処理を行うように
することで処理を効率よく行えるが、負荷変動に対して
課題が残る。即ち、嫌気性処理室に比較的大きな固形物
が入ると、嫌気性処理室内に溜まることがあり、このよ
うな時に気温上昇等によって嫌気性処理室内の固形物が
一気に溶解して下流側の好気性処理室等に流入すると、
好気性処理室の処理能力を超えてしまい、浄化不十分の
まま放流してしまうことになる。
DISCLOSURE OF THE INVENTION Problems to be Solved by the Invention
As disclosed in Japanese Unexamined Patent Application Publication No. JP-A No. 2003-242242, one treatment tank is divided into a plurality of chambers, and the anaerobic treatment and the aerobic treatment are performed in each chamber. Remains. That is, if a relatively large solid substance enters the anaerobic treatment chamber, it may be accumulated in the anaerobic treatment chamber. When flowing into the temper treatment chamber, etc.,
The treatment capacity of the aerobic treatment chamber will be exceeded, and it will be discharged with insufficient purification.

【0004】一方、特公昭58−15038号公報に開
示されるように、回転接触体で有機物の低分子化を行う
ことで大きな固形物をある程度細かくできるが、回転接
触体を処理室内に設けると、それだけ処理室の容積が制
限され所定量の処理を行うには浄化槽が大型化する。
On the other hand, as disclosed in Japanese Examined Patent Publication No. 58-15038, large solids can be made finer to some extent by lowering the molecular weight of organic substances in the rotary contact body. However, when the rotary contact body is provided in the processing chamber. The volume of the processing chamber is limited by that much, and the septic tank becomes large in size in order to perform a predetermined amount of processing.

【0005】[0005]

【課題を解決するための手段】上記課題を解決すべく本
発明は、浄化槽本体内を嫌気処理室、好気処理室、沈殿
室及び消毒室に画成した浄化槽の前記嫌気処理室の内部
若しくは外部に前曝気室を設け、この前曝気室に汚水管
を臨ませるとともに前曝気室と嫌気処理室とを連通せし
めた。
In order to solve the above problems, the present invention is directed to the inside of the anaerobic treatment chamber of the septic tank in which the septic tank main body is divided into an anaerobic treatment chamber, an aerobic treatment chamber, a precipitation chamber and a disinfection chamber. A pre-aeration chamber was provided outside, and a sewage pipe was exposed to this pre-aeration chamber and the pre-aeration chamber and the anaerobic treatment chamber were connected to each other.

【0006】[0006]

【作用】便所や洗面所、風呂、厨房などからの汚水は、
先ず前曝気室に入り、ここで大きな固形物は粉砕されて
小さくされ、更にある程度好気性処理がなされた状態で
嫌気性処理室に送られる。
[Function] Sewage from toilets, washrooms, baths, kitchens, etc.
First, it enters the pre-aeration chamber, where large solids are crushed and made smaller, and further sent to the anaerobic treatment chamber after being subjected to aerobic treatment to some extent.

【0007】[0007]

【実施例】以下に本発明の実施例を添付図面に基づいて
説明する。ここで、図1は本発明にかかる浄化槽の側断
面図、図2は同浄化槽の平断面図、図3は同浄化槽によ
る汚水の浄化のフローを示す図であり、先ず図1、図2
に基づいて浄化槽の構造を説明する。
Embodiments of the present invention will be described below with reference to the accompanying drawings. Here, FIG. 1 is a side sectional view of a septic tank according to the present invention, FIG. 2 is a plan sectional view of the septic tank, and FIG. 3 is a diagram showing a flow of purifying wastewater by the septic tank.
The structure of the septic tank will be described with reference to FIG.

【0008】浄化槽は本体1内を隔壁2…によって上流
側(図の左側)から順に、嫌気性処理室3、好気性処理
室4、沈殿室5及び消毒室6に画成され、嫌気性処理室
3内は更に隔壁7にて前曝気室8が画成され、この前曝
気室8には便所や厨房からの汚水流入管9が臨み、また
隔壁7に沿って前曝気室8の底部までエアーを吹込むた
めに先端部に散気管を備えた導入管10を設け、更に隔
壁7には嫌気性処理室3への連通口11を形成してい
る。尚、導入管10は好気性処理室4にも設けられてて
おり、エアーはブロワーを用いて吹込まれる。
The septic tank is divided into an anaerobic treatment chamber 3, an aerobic treatment chamber 4, a sedimentation chamber 5 and a disinfection chamber 6 in this order from the upstream side (left side in the figure) by the partition walls 2 ... In the chamber 3, a partition wall 7 further defines a front aeration chamber 8. The front aeration chamber 8 faces a wastewater inflow pipe 9 from a toilet or a kitchen, and along the partition wall 7 to the bottom of the front aeration chamber 8. An inlet pipe 10 having an air diffusing pipe is provided at the tip for blowing air, and a communication port 11 to the anaerobic treatment chamber 3 is formed in the partition wall 7. The introduction pipe 10 is also provided in the aerobic treatment chamber 4, and air is blown in using a blower.

【0009】嫌気性処理室3は下部で連通する2つの室
3a,3bに分けられ、各室3a,3bには合成樹脂等
の濾材に嫌気性菌が固定化された嫌気性濾床12を設け
ている。そして、嫌気性処理室3は隔壁2に設けた連通
口13にて好気性処理室4とつながっている。
The anaerobic treatment chamber 3 is divided into two chambers 3a and 3b which communicate with each other at the lower part, and each chamber 3a and 3b is provided with an anaerobic filter bed 12 in which anaerobic bacteria are immobilized on a filter material such as synthetic resin. It is provided. The anaerobic treatment chamber 3 is connected to the aerobic treatment chamber 4 through the communication port 13 provided in the partition wall 2.

【0010】好気性処理室4は隔壁14にて2つの室4
a,4bに分けられ、各室4a,4bは隔壁14に形成
した連通口15にてつながり、各室4a,4bには濾材
に好気性菌が固定化された好気性濾床16を設けてい
る。
The aerobic treatment chamber 4 is divided into two chambers 4 by a partition wall 14.
a) and 4b. The chambers 4a and 4b are connected to each other through a communication port 15 formed in the partition wall 14, and the chambers 4a and 4b are provided with an aerobic filter bed 16 in which aerobic bacteria are immobilized on the filter medium. There is.

【0011】ところで、前曝気室8と嫌気性処理室3a
とを画成する隔壁7、嫌気性処理室室3a,3bを画成
する隔壁2、好気性処理室4a,4bを画成する隔壁1
4及び好気性処理室4bと沈殿室5を画成する隔壁2に
沿って清掃口41,42,43,44を設けている。こ
れら清掃口41,42,43,44は濾床12,16よ
りも下方に開口している。
By the way, the pre-aeration chamber 8 and the anaerobic treatment chamber 3a
And a partition wall 7 defining the anaerobic treatment chambers 3a and 3b, and a partition wall 1 defining the aerobic treatment chambers 4a and 4b.
4 and cleaning ports 41, 42, 43, 44 are provided along the partition wall 2 that defines the aerobic treatment chamber 4b and the precipitation chamber 5. These cleaning ports 41, 42, 43, 44 are opened below the filter beds 12, 16.

【0012】沈殿室5は底面をロート状の傾斜面17と
して底部中央に汚泥を集める構造となっており、底部中
央の上方に筒状のセンターウェル18を固定し、このセ
ンターウェル18の外側に環状(四角形)の内側堰19
と鋸刃状の外側堰20を設け、これら内側堰19と外側
堰20間の溝に流出管21の一端を開口させ、他端を消
毒室6に開口せしめている。この消毒室6には消毒液を
供給する消毒器22と消毒後の処理液を外部に排出する
放流管23を設けている。
The bottom of the sedimentation chamber 5 has a funnel-shaped inclined surface 17 to collect sludge in the center of the bottom. A cylindrical center well 18 is fixed above the center of the bottom, and the center well 18 is placed outside the center well 18. Ring (square) inner weir 19
A saw-shaped outer weir 20 is provided, one end of the outflow pipe 21 is opened in the groove between the inner weir 19 and the outer weir 20, and the other end is opened in the disinfection chamber 6. The disinfection chamber 6 is provided with a disinfecting device 22 for supplying a disinfecting liquid and a discharge pipe 23 for discharging the processing liquid after the disinfection to the outside.

【0013】また、好気性処理室の下流側の室4bと沈
殿室5のセンターウェル18内部とはエアーリフトを利
用した定量移行装置24で連通し、更に、室4bとセン
ターウェル18間にはオーバーフロー管25が架設され
ている。
Further, the chamber 4b on the downstream side of the aerobic treatment chamber and the inside of the center well 18 of the precipitation chamber 5 are communicated with each other by a quantitative transfer device 24 using an air lift, and further, between the chamber 4b and the center well 18. An overflow pipe 25 is installed.

【0014】定量移行装置24はエアーリフト管24
a、このエアーリフト管24aの上端が接続する計量桝
24bと、この計量桝24bとセンターウェル18とを
つなぐか搬送管24cからなり、ブロワーにてエアーリ
フト管24a下部にエアーを吹込み、エアーの上昇とと
もに室4b内の液体を計量桝24b内に導入し、計量桝
24bに設けた開口或いは堰等を通して一定量の液体を
搬送管24cを介してセンターウェル18内に供給する
ようにしている。尚、処理水面が連通口15より下がっ
た場合には、電磁弁やフロート弁等の制御装置を用いて
ブロワーの運転を停止し、エアーリフトを止めることで
沈殿室5への処理水の流出を停止する。
The quantitative transfer device 24 is an air lift pipe 24.
a, a measuring container 24b to which the upper end of the air lift pipe 24a is connected, and a carrier pipe 24c that connects the measuring container 24b to the center well 18 and blows air to the lower part of the air lift pipe 24a with a blower As the temperature rises, the liquid in the chamber 4b is introduced into the measuring container 24b, and a constant amount of liquid is supplied into the center well 18 through the transfer pipe 24c through an opening or a weir provided in the measuring container 24b. .. When the treated water level drops below the communication port 15, the blower operation is stopped by using a control device such as a solenoid valve or a float valve, and the air lift is stopped to prevent the treated water from flowing into the settling chamber 5. Stop.

【0015】更に、センターウェル18の中心部には垂
直方向に吸引管26を挿通している。この吸引管26の
下端は沈殿室5の底面近くまで伸び、吸引管26の上端
には返送管27の基端が連結し、この返送管27の先端
は前記前曝気室8に開口している。そして、吸引管26
の下部にはポンプから伸びるエアー供給管28が接続
し、タイマー制御を行ない、一定時間経過後吸引管26
内にエアーを吹込むことでエアーリフト作用により汚泥
29を吸上げ、返送管27を介して汚泥29を前曝気室
8に戻すようにしている。尚、返送管27は自然に汚泥
が前曝気室8に戻るように前曝気室8に向かって若干傾
斜している。
Further, a suction tube 26 is vertically inserted through the center of the center well 18. The lower end of the suction pipe 26 extends to near the bottom surface of the settling chamber 5, the base end of the return pipe 27 is connected to the upper end of the suction pipe 26, and the front end of the return pipe 27 is open to the front aeration chamber 8. .. And the suction tube 26
An air supply pipe 28 extending from the pump is connected to the lower part of the pump to perform timer control, and after a certain time has elapsed, the suction pipe 26
By blowing air into the inside, the sludge 29 is sucked up by the air lift action, and the sludge 29 is returned to the front aeration chamber 8 through the return pipe 27. The return pipe 27 is slightly inclined toward the front aeration chamber 8 so that the sludge naturally returns to the front aeration chamber 8.

【0016】一方、前記好気性処理室4内にもエアーリ
フトを利用した移行装置30及び定量移行装置31を設
けている。移行装置30はエアーリフト管30a及び搬
送管30cからなり、定量移行装置31はエアーリフト
管31a、計量桝31b及び搬送管31cからなる。
On the other hand, a transfer device 30 and a fixed transfer device 31 utilizing an air lift are also provided in the aerobic treatment chamber 4. The transfer device 30 includes an air lift pipe 30a and a transfer pipe 30c, and the fixed amount transfer device 31 includes an air lift pipe 31a, a measuring container 31b, and a transfer pipe 31c.

【0017】定量移行装置31のエアーリフト管31a
下端は好気性処理室4b底部の中央部、つまり最も低い
部分に臨み、処理水とともに底部に溜まった汚泥を処理
水とともにエアーリフトの作用によって計量桝31bに
引き上げ、計量桝31bから一定量の汚泥を含む処理液
を搬送管31cを介して前記返送管27に送り込み、汚
泥を含む処理液の一部を前曝気室8を介して若しくは直
接前記嫌気性処理室3に戻すようにしている。
Air lift pipe 31a of the quantitative transfer device 31
The lower end faces the central part of the bottom of the aerobic treatment chamber 4b, that is, the lowest part. The sludge accumulated at the bottom together with the treated water is pulled up to the measuring basin 31b by the action of the air lift together with the treated water, and a certain amount of sludge is discharged from the measuring basin 31b. The treatment liquid containing the above is sent to the return pipe 27 via the carrier pipe 31c, and a part of the treatment liquid containing sludge is returned to the anaerobic treatment chamber 3 directly or through the pre-aeration chamber 8.

【0018】また、移行装置30についてはエアーリフ
ト管30aと搬送管30cとからなり、通常の浄化運転
の際にはエアーリフトを駆動せず、好気性処理室4a内
を清掃する場合のみ使用する。したがって定量移行のた
めの計量桝は省略している。
Further, the transfer device 30 is composed of an air lift pipe 30a and a transfer pipe 30c, and is used only when cleaning the inside of the aerobic treatment chamber 4a without driving the air lift during a normal cleaning operation. .. Therefore, the measuring cell for quantitative transfer is omitted.

【0019】以上の如き構成の浄化槽の作用を図3をも
参照して以下に述べる。先ず、便所や厨房からの汚水が
汚水流入管9を介して前曝気室8に流入すると、この前
曝気室8において汚水は攪拌され大きな固形物は小さく
粉砕され且つある程度好気性処理がなされる。
The operation of the septic tank having the above structure will be described below with reference to FIG. First, when sewage from a toilet or a kitchen flows into the pre-aeration chamber 8 through the sewage inflow pipe 9, the sewage is agitated in the pre-aeration chamber 8, large solids are pulverized into small pieces, and aerobic treatment is performed to some extent.

【0020】次いで、汚水は連通口11を介して嫌気性
処理室3内に送られる。この嫌気性処理室3において
は、先ず酸生成菌によって汚水中の有機物が酢酸(CH
3COOH)やプロピオン酸(CH3CH2COOH)等
の有機酸に低分子化される。そして更にこれら有機酸は
分解され、メタン菌などによってメタン(CH4)や二
酸化炭素(CO2)のガスと、タンパク質や尿素の窒素
分の分解物であるアンモニア態窒素(NH4 +)を含んだ
処理液を生成する。
Then, the sewage is sent into the anaerobic treatment chamber 3 through the communication port 11. In the anaerobic treatment chamber 3, first, the organic matter in the wastewater is converted to acetic acid (CH
3 COOH) and propionic acid (CH 3 CH 2 COOH) and other organic acids. Further, these organic acids are decomposed to contain gas of methane (CH 4 ) and carbon dioxide (CO 2 ) by methane bacteria and ammonia nitrogen (NH 4 + ) which is a decomposition product of nitrogen content of protein and urea. Produces a processing liquid.

【0021】このアンモニア態窒素(NH4 +)及び未分
解の有機物を含んだ処理液は連通口13を介して好気性
処理室4に送られる。好気性処理室4ではブロワーから
エアー導入管10を通して吹込まれた空気(酸素)を利
用して硝化菌などの好気性菌により酸化分解が行われ
る。この酸化分解によりアンモニア態窒素(NH4 +)は
硝酸態窒素(NO3 -)や亜硝酸態窒素(NO2 -)に酸化
分解される。
The treatment liquid containing the ammonia nitrogen (NH 4 + ) and the undecomposed organic matter is sent to the aerobic treatment chamber 4 through the communication port 13. In the aerobic treatment chamber 4, oxidative decomposition is performed by aerobic bacteria such as nitrifying bacteria using the air (oxygen) blown from the blower through the air introduction pipe 10. By this oxidative decomposition, ammonia nitrogen (NH 4 + ) is oxidatively decomposed into nitrate nitrogen (NO 3 ) and nitrite nitrogen (NO 2 ).

【0022】そして、硝酸態窒素(NO3 -)や亜硝酸態
窒素(NO2 -)を含む処理液の一部は吸引管31により
定量的に返送管27を介して嫌気性処理室3に戻され、
嫌気性処理室3内の脱窒菌によって分子状の窒素
(N2)や亜酸化窒素(N2O)に還元され、ガスとして
槽外へ排出される。このようにして硝酸態窒素(N
3 -)や亜硝酸態窒素(NO2 -)の濃度が低減した処理
水は沈殿室5に送られ、この沈殿室5の上澄み液が内側
堰19と外側堰20間の溝を通って消毒室6に送られ、
塩素消毒等を施された後に放流される。
A part of the treatment liquid containing nitrate nitrogen (NO 3 ) and nitrite nitrogen (NO 2 ) is quantitatively transferred to the anaerobic treatment chamber 3 by the suction pipe 31 via the return pipe 27. Returned,
It is reduced to molecular nitrogen (N 2 ) or nitrous oxide (N 2 O) by denitrifying bacteria in the anaerobic treatment chamber 3, and is discharged as a gas out of the tank. In this way, nitrate nitrogen (N
The treated water in which the concentrations of O 3 ) and nitrite nitrogen (NO 2 ) are reduced is sent to the precipitation chamber 5, and the supernatant liquid of the precipitation chamber 5 passes through the groove between the inner weir 19 and the outer weir 20. Sent to the disinfection room 6,
It is discharged after being sterilized with chlorine.

【0023】図4は別実施例に係る浄化槽の側断面図、
図5は図4に示した浄化槽の平断面図であり、この実施
例にあっては沈殿室5に沈殿室5の処理液表面に配設さ
れたスカムを収集する略漏斗形状のスカム収集部材45
aと、一端をスカム収集部材45aに、他端を前記返送
管27に連結したU字状配管45bとを備えたスカム収
集返送装置45を設け、このスカム収集部材45aにて
沈殿室5内の処理液表面に浮遊するスカムを吸引し、吸
引したスカムをエアリフト作用で返送管27に送り、返
送管27を介して前曝気室8に戻すようにしている。
FIG. 4 is a side sectional view of a septic tank according to another embodiment,
FIG. 5 is a plan sectional view of the septic tank shown in FIG. 4. In this embodiment, a substantially funnel-shaped scum collecting member that collects scum disposed on the surface of the processing liquid of the precipitation chamber 5 is set in the precipitation chamber 5. 45
and a scum collecting and returning device 45 provided with a scum collecting member 45a at one end and a U-shaped pipe 45b having the other end connected to the returning pipe 27. The scum floating on the surface of the treatment liquid is sucked, the sucked scum is sent to the return pipe 27 by the air lift action, and is returned to the front aeration chamber 8 via the return pipe 27.

【0024】図6は更なる別実施例に係る浄化槽の側断
面図、図7は図6に示した浄化槽の平断面図であり、こ
の実施例にあっては好気性処理室4bの処理液を沈殿室
に送る定量移行装置24、好気性処理室4bの汚泥を含
む処理液を返送管27に引き上げる定量移行装置31及
び清掃口44を全て好気性処理室4aと4bとを画成す
る隔壁14側に設けている。
FIG. 6 is a side sectional view of a septic tank according to still another embodiment, and FIG. 7 is a plan sectional view of the septic tank shown in FIG. 6. In this embodiment, the treatment liquid in the aerobic treatment chamber 4b is treated. For transferring the amount of sludge to the settling chamber, the quantitative transfer device 31 for pulling up the treatment liquid containing sludge in the aerobic treatment chamber 4b to the return pipe 27, and the cleaning port 44 are all partition walls defining the aerobic treatment chambers 4a and 4b. It is provided on the 14 side.

【0025】尚、図示例では好気処理室内の処理液の一
部を嫌気処理室へ送る処理液返送管と沈殿室内の汚泥を
前曝気室に戻す汚泥返送管とを共通の返送管としたが、
これらを別々にしてもよい。また、実施例では嫌気性処
理室の一部を凹所とし、この凹所を前曝気室としたが、
嫌気性処理室の側面等に突出した形状で前曝気室を取付
けるようにしてもよい。
In the illustrated example, the processing liquid return pipe for sending a part of the processing liquid in the aerobic treatment chamber to the anaerobic treatment chamber and the sludge returning pipe for returning the sludge in the settling chamber to the previous aeration chamber are common return pipes. But,
These may be separated. Further, in the embodiment, a part of the anaerobic treatment chamber is a recess, and this recess is a front aeration chamber,
The front aeration chamber may be attached to the side surface of the anaerobic treatment chamber so as to project.

【0026】[0026]

【発明の効果】以上に説明したように本発明によれば、
浄化槽の嫌気処理室の内部若しくは外部に前曝気室を設
け、この前曝気室で一旦汚水を受けて汚水中の固形物を
細かく粉砕し且つある程度好気性処理をして嫌気処理室
に送るようにしたので、大きな固形物や紙等が浄化槽に
入ってきても負荷変動を小さく抑えることができ、安定
した浄化を行うことができる。
As described above, according to the present invention,
A pre-aeration chamber is provided inside or outside the anaerobic treatment chamber of the septic tank, and once the sewage is received in this pre-aeration chamber, the solid matter in the sewage is finely crushed and aerobically treated to a certain degree and sent to the anaerobic treatment chamber. Therefore, even if a large solid matter, paper, or the like enters the septic tank, the load fluctuation can be suppressed to be small, and stable purification can be performed.

【0027】また、好気処理室内の処理液の一部を嫌気
処理室へ送り、窒素(N2)や亜酸化窒素(N2O)ガス
として槽外へ排出されることで嫌気性菌や好気性菌の活
性を抑制するアンモニア態窒素や硝酸態窒素、亜硝酸態
窒素が過剰に増加するのを防止できるため、安定した浄
化を行なうことができる。更に好気処理室内の処理液の
一部を嫌気処理室へ送る処理液返送管と沈殿室内の汚泥
を前曝気室に戻す汚泥返送管を共用することで、沈殿室
の底部から汚泥を嫌気処理室に返送することができ、浄
化槽外へ固形物を除去する必要がなくなるため、メンテ
ナンスが簡単になり、浄化槽自体の構造の簡略化を図る
こともできる。
Further, a part of the treatment liquid in the aerobic treatment chamber is sent to the anaerobic treatment chamber and discharged as nitrogen (N 2 ) or nitrous oxide (N 2 O) gas to the outside of the anaerobic bacteria. Since it is possible to prevent an excessive increase of ammonia nitrogen, nitrate nitrogen, and nitrite nitrogen that suppress the activity of aerobic bacteria, it is possible to perform stable purification. Furthermore, by sharing the processing liquid return pipe that sends part of the processing liquid in the aerobic treatment chamber to the anaerobic treatment chamber and the sludge return pipe that returns the sludge in the sedimentation chamber to the previous aeration chamber, sludge is anaerobically treated from the bottom of the sedimentation chamber. Since it can be returned to the chamber and the solid matter does not need to be removed to the outside of the septic tank, maintenance is simplified and the structure of the septic tank itself can be simplified.

【0028】また、好気性処理室から沈殿室への処理液
の移行を定量移行装置を介して行なうことで、安定した
運転を行なうことが可能となり、定量移行装置を好気性
処理室を画成する隔壁に沿って設け、更に清掃口も隔壁
に沿って設けることで構造が簡単になり、製造しやすく
なる。特に好気性処理室を2つの室に分割し、それぞれ
の室に清掃口を設けることで、清掃しやすくなる。
Further, since the processing liquid is transferred from the aerobic treatment chamber to the precipitation chamber through the quantitative transfer device, stable operation can be performed, and the quantitative transfer device defines the aerobic treatment chamber. By arranging the cleaning port along the partition wall and the cleaning port also along the partition wall, the structure becomes simple and the manufacturing becomes easy. In particular, the aerobic treatment chamber is divided into two chambers, and a cleaning port is provided in each chamber to facilitate cleaning.

【0029】更に、沈殿室にスカム収集返送装置を設
け、沈殿室に浮遊するスカムを前曝気室或いは嫌気性処
理室に戻すようにすれば、定期的にスカムを除去する作
業が不要になる。
Further, if a scum collecting and returning device is provided in the settling chamber and the scum floating in the settling chamber is returned to the pre-aeration chamber or the anaerobic treatment chamber, the work of removing the scum periodically becomes unnecessary.

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

【図1】本発明に係る浄化槽の側断面図FIG. 1 is a side sectional view of a septic tank according to the present invention.

【図2】同浄化槽の平断面図FIG. 2 is a plan sectional view of the septic tank.

【図3】同浄化槽による汚水の浄化のフローを示す図FIG. 3 is a diagram showing a flow of purifying wastewater by the septic tank.

【図4】別実施例に係る浄化槽の側断面図FIG. 4 is a side sectional view of a septic tank according to another embodiment.

【図5】図4に示した浄化槽の平断面図5 is a plan sectional view of the septic tank shown in FIG.

【図6】別実施例に係る浄化槽の側断面図FIG. 6 is a side sectional view of a septic tank according to another embodiment.

【図7】図6に示した浄化槽の平断面図FIG. 7 is a plan sectional view of the septic tank shown in FIG.

【符号の説明】[Explanation of symbols]

1…浄化槽本体、2,7,14…隔壁、3…嫌気性処理
室、4…好気性処理室、5…沈殿室、6…消毒室、8…
前曝気室、10…エアー導入管、11,13,15…連
通口、12,13…濾床、24,31…定量移行装置、
27…返送管、41,42,43,44…清掃口、45
…スカム収集返送装置。
1 ... Septic tank main body, 2, 7, 14 ... Partition wall, 3 ... Anaerobic treatment chamber, 4 ... Aerobic treatment chamber, 5 ... Sedimentation chamber, 6 ... Disinfection chamber, 8 ...
Front aeration chamber, 10 ... Air introduction pipe, 11, 13, 15 ... Communication port, 12, 13 ... Filter bed, 24, 31 ... Fixed amount transfer device,
27 ... Return pipe, 41, 42, 43, 44 ... Cleaning port, 45
… Scum collecting and returning device.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 西村 勝己 福岡県北九州市小倉北区中島2丁目1番1 号 東陶機器株式会社内 (72)発明者 辻 隆正 福岡県北九州市小倉北区中島2丁目1番1 号 東陶機器株式会社内 (72)発明者 竹崎 義則 福岡県北九州市小倉北区中島2丁目1番1 号 東陶機器株式会社内 (72)発明者 河野 秀平 福岡県北九州市小倉北区中島2丁目1番1 号 東陶機器株式会社内 (72)発明者 沖 弘敏 石川県金沢市西泉3丁目92番地 アムズ株 式会社内 (72)発明者 酒谷 孝宏 石川県金沢市西泉3丁目92番地 アムズ株 式会社内 (72)発明者 関上 佳秀 石川県金沢市西泉3丁目92番地 アムズ株 式会社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Katsumi Nishimura 2-1-1 Nakajima, Kokurakita-ku, Kitakyushu, Fukuoka Prefecture Totoki Kikai Co., Ltd. (72) Takamasa Tsuji 2 Nakajima, Kokurakita-ku, Kitakyushu, Fukuoka 1st, 1st Totoki Co., Ltd. (72) Inventor Yoshinori Takezaki 2-1-1, Nakajima, Kokurakita-ku, Kitakyushu, Kitakyushu, Fukuoka (72) Inventor, Shuhei Kono Kokura Kitakyushu, Fukuoka 2-1-1 Nakajima, Kita-ku Totoki Equipment Co., Ltd. (72) Hirotoshi Oki 3-92 Nishiizumi, Kanazawa-shi, Ishikawa Prefecture In Ams Co., Ltd. (72) Takahiro Sakata 3-chome Nishizumi, Kanazawa-shi, Ishikawa Prefecture Address 92 Ams stock company (72) Inventor Yoshihide Sekigami 3-chome, Nishizumi, Kanazawa, Ishikawa Prefecture 92 Ams stock company

Claims (7)

【特許請求の範囲】[Claims] 【請求項1】 浄化槽本体内を嫌気性処理室、好気性処
理室、沈殿室及び消毒室に画成した浄化槽において、前
記嫌気性処理室の内部若しくは外部に前曝気室を設け、
この前曝気室に汚水流入管を臨ませるとともに前曝気室
と嫌気性処理室とを連通せしめたことを特徴とする浄化
槽。
1. A septic tank in which the inside of the septic tank main body is divided into an anaerobic treatment chamber, an aerobic treatment chamber, a precipitation chamber and a disinfection chamber, and a pre-aeration chamber is provided inside or outside the anaerobic treatment chamber,
A septic tank characterized in that a sewage inflow pipe is exposed to the front aeration chamber and the front aeration chamber and the anaerobic treatment chamber are communicated with each other.
【請求項2】 前記嫌気性処理室と好気性処理室との間
には好気性処理室内の処理液の一部を嫌気性処理室へ送
る処理液返送管が設けられていることを特徴とする請求
項1に記載の浄化槽。
2. A treatment liquid return pipe for feeding a part of the treatment liquid in the aerobic treatment chamber to the anaerobic treatment chamber is provided between the anaerobic treatment chamber and the aerobic treatment chamber. The septic tank according to claim 1.
【請求項3】 前記前曝気室と沈殿室との間には沈殿室
内の汚泥を前曝気室に戻す汚泥返送管が設けられ、この
汚泥返送管が処理液返送管を兼ねることを特徴とする請
求項2に記載の浄化槽。
3. A sludge return pipe for returning sludge in the settling chamber to the front aeration chamber is provided between the pre-aeration chamber and the settling chamber, and the sludge return pipe also serves as a treatment liquid return pipe. The septic tank according to claim 2.
【請求項4】 前記好気性処理室を画成する壁面に沿っ
て好気性処理室内の液体を沈殿室に一定量ずつ移行する
定量移行装置を配設したことを特徴とする請求項1に記
載の浄化槽。
4. The quantitative transfer device for transferring a constant amount of liquid in the aerobic treatment chamber to the settling chamber along a wall surface defining the aerobic treatment chamber, according to claim 1. Septic tank.
【請求項5】 前記好気性処理室は2つの室に分割さ
れ、各室を画成する壁面に沿って濾床の下方に開口する
清掃口を設けたことを特徴とする請求項1に記載の浄化
槽。
5. The aerobic treatment chamber is divided into two chambers, and a cleaning port that opens below the filter bed is provided along a wall surface that defines each chamber. Septic tank.
【請求項6】 前記好気性処理室には好気性処理室内の
汚泥を前記処理液返送管に一定量づつ移行する定量移行
装置を配設したことを特徴とする請求項2に記載の浄化
槽。
6. The septic tank according to claim 2, wherein the aerobic treatment chamber is provided with a fixed amount transfer device for transferring sludge in the aerobic treatment chamber to the treatment liquid return pipe by a predetermined amount.
【請求項7】 前記沈殿室には浮遊するスカムを収集し
前記汚泥返送管を介して前曝気室に戻すスカム収集返送
装置を設けたことを特徴とする請求項3に記載の浄化
槽。
7. The septic tank according to claim 3, wherein the settling chamber is provided with a scum collecting and returning device for collecting floating scum and returning it to the previous aeration chamber through the sludge returning pipe.
JP25536692A 1992-03-23 1992-09-01 Septic tank Withdrawn JPH05317872A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP25536692A JPH05317872A (en) 1992-03-23 1992-09-01 Septic tank

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP2417092 1992-03-23
JP4-24170 1992-03-23
JP25536692A JPH05317872A (en) 1992-03-23 1992-09-01 Septic tank

Publications (1)

Publication Number Publication Date
JPH05317872A true JPH05317872A (en) 1993-12-03

Family

ID=26361655

Family Applications (1)

Application Number Title Priority Date Filing Date
JP25536692A Withdrawn JPH05317872A (en) 1992-03-23 1992-09-01 Septic tank

Country Status (1)

Country Link
JP (1) JPH05317872A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100459331B1 (en) * 2002-12-09 2004-12-03 대명엔텍(주) Sweage disposal equipment being highly processing type with aspirated diffusers for recirculating sludge using by air stone
JP2007136378A (en) * 2005-11-21 2007-06-07 Hitachi Housetec Co Ltd Septic tank
WO2011118747A1 (en) * 2010-03-26 2011-09-29 株式会社クボタ Wastewater treatment device and wastewater treatment method

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100459331B1 (en) * 2002-12-09 2004-12-03 대명엔텍(주) Sweage disposal equipment being highly processing type with aspirated diffusers for recirculating sludge using by air stone
JP2007136378A (en) * 2005-11-21 2007-06-07 Hitachi Housetec Co Ltd Septic tank
WO2011118747A1 (en) * 2010-03-26 2011-09-29 株式会社クボタ Wastewater treatment device and wastewater treatment method

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