JPH02222780A - Structure of collecting inlet chamber of septic tank - Google Patents

Structure of collecting inlet chamber of septic tank

Info

Publication number
JPH02222780A
JPH02222780A JP4394589A JP4394589A JPH02222780A JP H02222780 A JPH02222780 A JP H02222780A JP 4394589 A JP4394589 A JP 4394589A JP 4394589 A JP4394589 A JP 4394589A JP H02222780 A JPH02222780 A JP H02222780A
Authority
JP
Japan
Prior art keywords
chamber
pipe
treated water
air
water
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.)
Pending
Application number
JP4394589A
Other languages
Japanese (ja)
Inventor
Shuhei Kono
秀平 河野
Katsumi Nishimura
勝己 西村
Sadami Ootsubo
大坪 貞視
Isao Miura
三浦 勲
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.)
Toto Ltd
Original Assignee
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 Toto Ltd filed Critical Toto Ltd
Priority to JP4394589A priority Critical patent/JPH02222780A/en
Publication of JPH02222780A publication Critical patent/JPH02222780A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To adequately maintain the activity of anaerobic bacteria by lifting a part of the treated water during the decomposition treatment in an aerobic treatment chamber by the air lift effect of an air lift pipe into a collecting inlet chamber and returning only the specified volume thereof into an anaerobic treatment. CONSTITUTION:Air is supplied into the treated water from an air diffusion pipe 13b and the treated water under the aerobic decomposition treatment is lifted partly into the collecting inlet chamber 40 in the aerobic treatment chamber a3 by the air lifting effect of an air lift pipe 14. The specified volume of the water is returned via a triangular weir in the collecting inlet chamber 40 into the 1st chamber a1 of the anaerobic treatment chamber C through a reflux pipe 70 so that the decomposition treatment of org. matter is executed by not only the anaerobic bacteria but a part of the reflux water and the denitrifying bacteria thereof as well. The volume of the transfer from the anaerobic treatment chamber C to the aerobic treatment chamber a3 is regulated to the volume obtd. by adding the specified volume of the reflux water to the volume of the treated water flowing from a sewage discharge pipeline D. The treated water is released from a release port 17 through a settling separating chamber a4 and a disinfecting chamber 18. The activity of the anaerobic bacteria is maintained always adequately in this way and the efficiency of the treatment to decompose the org. matter is improved.

Description

【発明の詳細な説明】 (イ) 産業上の利用分野 本発明は、浄化槽における集水桝構造に関するものであ
る。
DETAILED DESCRIPTION OF THE INVENTION (a) Field of Industrial Application The present invention relates to a water catchment structure in a septic tank.

(ロ) 従来の技術 従来、浄化槽の一形態として、実開昭63−45894
号公報に記載のものがある。
(b) Conventional technology Traditionally, as a form of septic tank, Utility Model Application No. 63-45894
There is something described in the publication.

すなわち、上記浄化槽は、第15図に示すように、浄化
槽本体(90)内に、汚水が流入する第1@。
That is, in the septic tank, as shown in FIG. 15, the septic tank has a first part into which wastewater flows into the septic tank main body (90).

気性処理室(91)と、同第1嫌気性処理室(91)で
嫌気性処理された汚水が流入する第2嫌気性処理室(9
2)と、同第2嫌気性処理室(92)でさらに嫌気性処
理された汚水が流入する好気性処理室(93)と、同好
気性処理室(93)で好気性処理された汚水が流入する
沈澱分離室(94)と、同沈澱分離室(94)で分離さ
れた上澄み液が流入する消毒室(95)とから構成して
いる。
an anaerobic treatment chamber (91) and a second anaerobic treatment chamber (9) into which wastewater anaerobically treated in the first anaerobic treatment chamber (91) flows.
2), an aerobic treatment chamber (93) into which sewage that has been further anaerobically treated in the second anaerobic treatment chamber (92) flows in, and sewage that has been aerobically treated in the same aerobic treatment chamber (93) flows into it. It consists of a precipitation separation chamber (94) in which the precipitation separation chamber (94) is separated, and a disinfection chamber (95) into which the supernatant liquid separated in the precipitation separation chamber (94) flows.

(ハ) 発明が解決しようとする課題 ところが、上記浄化槽の場合、第1・第2嫌気性処理室
(91)(92)において、有機態窒素が嫌気分解され
て発生するアンモニア態の窒素の濃度が高くなると嫌気
性菌の活性が抑制されて、嫌気性処理能力が低下すると
いう問題が生じていた。
(c) Problems to be Solved by the Invention However, in the case of the above-mentioned septic tank, the concentration of ammonia nitrogen generated by anaerobic decomposition of organic nitrogen in the first and second anaerobic treatment chambers (91) and (92). When this value becomes high, the activity of anaerobic bacteria is suppressed, resulting in a problem that the anaerobic treatment capacity decreases.

(ニ) 課題を解決するための手段 そこで、本発明では、好気性処理室内の下部に散気管を
配設し、同散気管の上方にエアリフト管の下端を開口す
ると共に、同エアリフト管の上端を集水桝を介して嫌気
性処理室内と連通させ、散気管にエア配管を介して空気
を供給することにより、同散気管より処理水中に空気を
供給し、上記エアリフト管のエアリフト作用により好気
性処理室内で好気性分解処理中の処理水の一部を、集水
桝内に押上げると共に、同集水桝より一定量たけ連続し
て嫌気性処理室に還流させるように構成した浄化槽にお
ける集水桝構造を提供せんとするものである。
(d) Means for Solving the Problems Therefore, in the present invention, an aeration pipe is arranged at the lower part of the aerobic treatment chamber, the lower end of the air lift pipe is opened above the aeration pipe, and the upper end of the air lift pipe is opened above the aeration pipe. is communicated with the anaerobic treatment chamber via a water collection basin, and air is supplied to the aeration pipe through the air piping, thereby supplying air into the treated water from the aeration pipe, which is preferable due to the air lift action of the air lift pipe. In a septic tank configured so that a part of the treated water undergoing aerobic decomposition treatment in the aerobic treatment chamber is pushed up into a water collection basin, and a certain amount of water is continuously returned from the collection basin to the anaerobic treatment chamber. The purpose is to provide a water catchment structure.

まな、集水桝を略箱形状に形成し、同集水桝の一側壁に
嫌気性処理室と連通ずる連通口を開口すると共に、同集
水桝の他側壁にオーバーフロニ開口部を切欠形成し、か
つ集水桝の底面よりオーバーフロー開口部の下端縁よで
の高さを、集水桝の底面より連通口の下端縁までの高さ
よりも高くして、集水桝の底面に連通連結したエアリフ
ト管中を通して集水桝内に押上げられてくる好気性分解
処理中の処理水の一部を一定量だけ連通口を通して嫌気
性処理室へ還流可能としたことにも特徴を有する。
The water collection basin is formed into a substantially box shape, and a communication port communicating with the anaerobic treatment chamber is opened in one side wall of the water collection basin, and an overflow opening is cut out in the other side wall of the same water collection basin. and the height from the bottom of the catch basin to the lower edge of the overflow opening is higher than the height from the bottom of the catch basin to the lower edge of the communication opening, so that it is connected to the bottom of the catch basin. Another feature is that a certain amount of the treated water during the aerobic decomposition process, which is pushed up into the water collection basin through the air lift pipe, can be returned to the anaerobic treatment chamber through the communication port.

(ホ) 実施例 本発明の実施例を図面にもとづき詳説すれば、第1図及
び第2図において(^)は家庭用の浄化槽を示しており
、同浄化槽(A)は浄化槽本体(a)と蓋体(b)とか
ら構成し、家庭の便所や厨房等からの汚水を゛排出する
管路の中途に介設している。
(E) Embodiment The embodiment of the present invention will be explained in detail based on the drawings. In Figs. 1 and 2, (^) indicates a domestic septic tank, and the septic tank (A) is the septic tank body (a). and a lid body (b), and is installed in the middle of a pipe that discharges wastewater from a household toilet, kitchen, etc.

浄化槽本体(a)は、第1図〜第3図に示すように、上
面開放の略箱型であり、内部を隔壁(1)+2)(3)
を長手方向に一定間隔を開けて立設することにより、内
部空間を、嫌気性処理室(C)を形成する第1室(al
)、第2室(a2)と、好気性処理室(a3)と、内部
に消毒室(18)を配設した沈澱分離室(a4)とに区
画している。
As shown in Figures 1 to 3, the septic tank body (a) is approximately box-shaped with an open top, and the inside is partitioned into partitions (1) + 2) (3).
are set upright at regular intervals in the longitudinal direction, the internal space is divided into a first chamber (al) forming an anaerobic treatment chamber (C).
), a second chamber (a2), an aerobic treatment chamber (a3), and a sedimentation separation chamber (a4) in which a disinfection chamber (18) is provided.

第1室(al)は、汚水排出管路(D)の上流側と流入
口(4)を介して連通しており、流入口(4)は、略横
]゛字形状で汚水排出管路(0)から第1室(al)に
流入する汚水(以下「処理水」という)を下方向に折曲
り状に案内するようにしている。
The first chamber (al) communicates with the upstream side of the sewage discharge pipe (D) via an inlet (4), and the inlet (4) has a substantially horizontal ゛ shape and is connected to the sewage discharge pipe. The wastewater (hereinafter referred to as "treated water") flowing into the first chamber (al) from (0) is guided downward in a curved manner.

また、上記流入口(4)の直下方には、第2室(a2)
側に向けて前低後高に傾斜させた邪魔板(25)を配設
して、流入口(4)より流入してくる汚水を、同邪魔板
(25)に沿わせて後述する下向流嫌気性炉床(5)上
に落下させるようにしている。(26)は邪魔板ステー
である。
Also, directly below the inlet (4) is a second chamber (a2).
A baffle plate (25) that is inclined toward the side with a lower front and a higher rear is arranged to direct the wastewater flowing in from the inlet (4) along the baffle plate (25) in a downward direction as described below. It is made to fall onto the flowing anaerobic hearth (5). (26) is a baffle plate stay.

このように、邪魔板(25)を配設することにより、処
理水が第1室(1a)内を直線的に通過して浄化処理が
行なわれないという不具合の発生の防止と、処理水の直
線的な流入による嫌気性処理を行なう第1室(al)内
への空気の巻込み混入の防止と、第1室(al)内の処
理水面に形成されたスカム層の破壊による空気接触の防
止と、騒音の発生防止を図っている。
In this way, by arranging the baffle plate (25), it is possible to prevent the problem that the treated water passes straight through the first chamber (1a) and the purification process is not performed, and also to prevent the treated water from being purified. Prevention of air entrainment into the first chamber (al) where anaerobic treatment is performed by linear inflow, and prevention of air contact by destruction of the scum layer formed on the treated water surface in the first chamber (al). Efforts are being made to prevent the occurrence of noise.

また、第1室(al)中には、流入口(4)がら下方向
に所定間隔を設けて下向流嫌気性炉床(5)を設けてお
り、同下向流嫌気性炉床(5)は、浄化槽本体(a)及
び隔壁(1)の内側面に固設した支持体(6)(6“)
の上下にそれぞれ格子状の上下部P材棚(7)(7°)
を張設し、同上下部炉材棚(7)(7°)間に嫌気性菌
を付着させたP材を充填して構成している。
Further, in the first chamber (al), a downward flow anaerobic hearth (5) is provided at a predetermined interval downward from the inlet (4). 5) is a support (6) (6") fixed to the inner surface of the septic tank body (a) and the partition wall (1).
Upper and lower P material shelves (7) (7°) with lattice-like patterns on the top and bottom of the
is stretched, and P material to which anaerobic bacteria is attached is filled between the upper and lower furnace material shelves (7) (7 degrees).

炉材は、合成樹脂やその他の素材により表面積及び空隙
率を著しく高めるように形成している。
The furnace material is made of synthetic resin or other materials to significantly increase its surface area and porosity.

第2室(a2)は、内部に上向流嫌気性炉床(9)を収
容しており、前記の下向流嫌気性炉床(5)と略同−梢
遣であるが、枦林間の空隙率をより小さくし、表面積を
より大きくしたことが前記炉床(5)と異なる。 (8
)(8’)は上下部沢材棚、(8a)(8b)は支持体
である。
The second chamber (a2) accommodates an upward flow anaerobic hearth (9) inside, and is approximately the same as the above-mentioned downward flow anaerobic hearth (5). It differs from the hearth (5) in that it has a smaller porosity and a larger surface area. (8
) (8') are upper and lower baffle shelves, (8a) and (8b) are supports.

特に、第1室(al)と第2室(a2)を分割した隔壁
(1)は、浄化槽本体(a)内の処理水面(h)よりも
下方を完全に仕切っており、第1室(al)から第2室
(a2)への処理水の移流は、隔壁(1)の第1室(a
l)ff+!!と第2室(a2)側の側面に沿って立設
した第1・第2移流管(1o)(H)中を通して行われ
る。
In particular, the partition wall (1) that divides the first chamber (al) and the second chamber (a2) completely partitions the area below the treated water level (h) in the septic tank body (a), and the first chamber ( Advection of the treated water from the first chamber (a2) of the partition wall (1) to the second chamber (a2)
l)ff+! ! This is carried out through the first and second advection pipes (1o) (H) that are installed upright along the side surface of the second chamber (a2).

第1・第2移流管(10)(11)は、第3図に示すよ
うに、それぞれ断回路■、字形状に形成し、隔壁(1)
をはさんで対称位置に、それぞれ一方の端縁を隔!(1
)の側面に密接させると共に、それぞれ他方の端縁を浄
化槽本体(a)の側壁(20)の内面に密接させて、上
下端がそれぞれ各炉床(5)(9)の上下方で開放した
管体を形成し、各移流管(10011)間の隔壁(1)
に、上方から処理水面(h)よりもやや低位置に達する
略方形状の連通口(21)を切欠いて第1室(al)と
第2室(a2)とを連通させている。
As shown in FIG.
In a symmetrical position with one edge separated from each other! (1
), the other edge of each was brought into close contact with the inner surface of the side wall (20) of the septic tank body (a), and the upper and lower ends were open above and below each hearth (5) and (9), respectively. A partition wall (1) forming a tube body and between each advection tube (10011)
A substantially rectangular communication port (21) extending from above to a position slightly lower than the treated water level (h) is cut out to communicate the first chamber (al) and the second chamber (a2).

そして、かかる第1・第2移流管(10)(11)は、
前記流入口(4)から等距離に位置するように、隔壁(
1)の左右側に各1組、計2組配設し、第1室(al)
と第2室(a2)とを連通ずる連通口(21)も、左右
一対設けて、各連通口(21)に、可動せき(3o)を
上下方向へスライド調節可能に取付けている。
The first and second advection pipes (10) and (11) are
A partition wall (
1), one set each on the left and right sides, a total of two sets, and the first room (al)
A pair of communication ports (21) are also provided on the left and right to communicate between the first chamber and the second chamber (a2), and a movable weir (3o) is attached to each communication port (21) so as to be slidable in the vertical direction.

そして、可動せき(30)は、連通口(21)の横幅よ
りもやや幅広の矩形板状に形成し、上端縁(30a )
を鋸歯状に形成しており、隔壁(1)に近接する浄化槽
本体(a)の側! (20)の内面と、同内面と対向す
る第2移流管(11)の側壁内面とにそれぞれ設けたガ
イドレール(31)(31°)中に上下スライド自在に
嵌入している。
The movable weir (30) is formed into a rectangular plate shape slightly wider than the width of the communication port (21), and has an upper edge (30a).
The side of the septic tank body (a) that is close to the partition wall (1) is formed into a sawtooth shape! (20) and the inner surface of the side wall of the second advection tube (11) facing the same inner surface, respectively, are fitted into guide rails (31) (31°) so as to be vertically slidable.

しかも、可動せき(30)の中央部には、下端より中央
部にかけて縦長に調節ボルト摺動溝(32)を切欠形成
し、同摺動溝(32)中を通して隔壁(1)にスライド
調節ボルト(33)を挿通し、同調節ボルト(33)の
先端に調節つまみ付ナツト(34)を締付調節自在に螺
着して、同ナツト(34)の締付調節により可動せき(
30)を上下スライド・固定させて、上下位置調節が行
なえるようにしている。(35)は固定板である。
In addition, a vertical adjustment bolt sliding groove (32) is formed in the center of the movable weir (30) from the lower end to the center, and the sliding adjustment bolt is passed through the sliding groove (32) and attached to the partition wall (1). (33), and screw a nut (34) with an adjustment knob onto the tip of the adjustment bolt (33) so that the tightening can be freely adjusted.
30) is slid and fixed up and down so that the vertical position can be adjusted. (35) is a fixed plate.

次に、好気性処理室(a3)の構成について説明する。Next, the configuration of the aerobic treatment chamber (a3) will be explained.

まず、第1図を参照して、嫌気性処理室(C)の第2室
(a2)から好気性処理室(a3)に処理水を移送する
構成について説明すると、第2室(a2)と好気性処理
室(a3)間の隔壁(2)は、浄化槽本体(a)の処理
水面(h)よりも下方を完全に仕切っており、第2室(
a2)から好気性処理室(a3)への処理水の移流は、
間隔u(2)の第2室(a2)側の側面に設けた第3移
流管(16)により行われる。
First, referring to FIG. 1, the configuration for transferring treated water from the second chamber (a2) of the anaerobic treatment chamber (C) to the aerobic treatment chamber (a3) will be explained. The partition wall (2) between the aerobic treatment chambers (a3) completely partitions the area below the treated water level (h) of the septic tank body (a), and separates the second chamber (
The advection of treated water from a2) to the aerobic treatment room (a3) is as follows:
This is performed by the third advection pipe (16) provided on the side surface of the second chamber (a2) at the interval u(2).

第3移流管(16)は、上下端開放の断面略コ字状に形
成し、同コ字形状断面の開口端縁を隔壁(2)の第2室
(a2)側側面に密接させて、下端が上向流嫌気性炉床
(9)の上方で開口し、上端が処理水面(h)よりも上
方で開口した第3移流管(16)の管体を形成し、隔壁
(2)に略方形状の移流口(16a)を開口して第2室
(a2)と好気性処理室(a3)とを各室(a2Ha3
)の上部で連通させている。
The third advection pipe (16) is formed in a substantially U-shaped cross section with open upper and lower ends, and the opening edge of the U-shaped cross section is brought into close contact with the side surface of the partition wall (2) on the second chamber (a2) side. A third advection tube (16) whose lower end opens above the upward flow anaerobic hearth (9) and whose upper end opens above the treated water level (h) is formed, and is connected to the partition wall (2). The substantially rectangular advection port (16a) is opened to connect the second chamber (a2) and the aerobic treatment chamber (a3) to each chamber (a2Ha3).
) are connected at the top.

好気性処理室(a3)は、第1図、第3図及び第4図に
示すように、内部に好気性炉床(12)、曝気装置(1
3)、エアリフト管(14)、逆洗管(15)を内蔵し
ている。(なお、エアリフト管(14)は、後述する処
理水一部還流装置(E)の一部を構成するものであるな
め、間装! (E)の説明の個所で説明する。)まず、
好気性炉床(12)について説明すると、同好気性炉床
(12)は、好気性処理室(a3)中に内底面から所定
間隔を開けて沈設した枠体(12a)に、中心紐に繊維
質の枦糸多数を略房状に取付けて形成した紐状沢材(1
2b)を多数支持させ、同紐状沢材(12b)に好気性
菌を付着させて構成している。
As shown in FIGS. 1, 3, and 4, the aerobic treatment chamber (a3) has an aerobic hearth (12) and an aeration device (1) inside.
3), an air lift pipe (14), and a backwash pipe (15) are built-in. (The air lift pipe (14) is a part of the treated water partial recirculation device (E), which will be described later, and will be explained in the explanation section (E).) First,
To explain the aerobic hearth (12), the aerobic hearth (12) has a frame (12a) sunk in the aerobic treatment chamber (a3) at a predetermined distance from the inner bottom surface, and a fiber attached to the center string. A string-like material (1
2b), and aerobic bacteria are attached to the string-like swamp material (12b).

また、好気性炉床の炉材として、本発明では紐状炉材(
12b)を用いたが、他に波板状、ハニカム状でもよい
。
In addition, in the present invention, string-shaped furnace material (
12b) was used, but a corrugated plate shape or a honeycomb shape may also be used.

曝気装置(13)は、第2室(a2)と好気性処理室(
a3)間の隔壁(2)に沿って垂設したエア縦管(13
a)の下端から左右側方に、それぞれ多数のエア噴出孔
(13d)を軸線方向に一定間隔を開けて設けた散気管
(13b)[13b)を略水平状に連通連設して、エア
縦管(13a)の上端にエア配管(t3c)を介して供
給される空気を、同エア噴出口(13d)より処理水中
に供給するようにしている。
The aeration device (13) has a second chamber (a2) and an aerobic treatment chamber (
Air vertical pipe (13) installed vertically along the partition wall (2) between a3)
Aeration pipes (13b) [13b] each having a large number of air jet holes (13d) provided at regular intervals in the axial direction are connected in a substantially horizontal manner from the lower end to the left and right sides of a), and the air is Air is supplied to the upper end of the vertical pipe (13a) via an air pipe (t3c) and is supplied into the treated water from the air outlet (13d).

かかる構成によって、エア縦管(13a)及び散気管(
13bH13b)を通して空気を好気性処理室(a3)
内に供給することができ、好気性菌の活性を保持するこ
とができる。
With this configuration, the vertical air pipe (13a) and the air diffuser pipe (
13bH13b) through the aerobic treatment chamber (a3)
It is possible to maintain the activity of aerobic bacteria.

また、エア配管(13C)の中途部には、散気管(13
b)に供給するエア量を調節するためのエア旦調節部(
50)と、散気管(13b)へ供給する空気を後述する
逆洗管(15)へ切換えて供給するための三方ボールバ
ルブ(55)を設けている。
In addition, a diffuser pipe (13C) is installed in the middle of the air pipe (13C).
b) An air adjustment unit for adjusting the amount of air supplied to (
50) and a three-way ball valve (55) for switching and supplying the air supplied to the diffuser pipe (13b) to a backwash pipe (15) to be described later.

よた、左右の散気管(13bH13b)の直上方で処理
水面(h)の近傍には、それぞれ対流ガイド板(60)
(61)を配設しており、各対流ガイド板(60)(6
1)は、下端部を隔u(2)に支持部材(62)(63
)により固定し、中途部を上方へ凸状に弯曲させて、上
端を処理水面(h)に近接させている。
Also, there are convection guide plates (60) directly above the left and right air diffusers (13bH13b) and near the treated water surface (h).
(61) are arranged, and each convection guide plate (60) (6
1) has supporting members (62) (63) with their lower ends separated by u(2).
), and the middle part is curved upward in a convex manner, and the upper end is brought close to the treated water surface (h).

従って、散気管(13b)(13b)から噴出される散
気による好気性処理室(a3)内の処理水の対流を促進
し、好気性菌への空気の供給を促進することができる。
Therefore, the convection of the treated water in the aerobic treatment chamber (a3) by the air diffused from the air diffuser pipes (13b) (13b) can be promoted, and the supply of air to the aerobic bacteria can be promoted.

しかも、各対流ガイド板(60) +61)の下端部と
隔壁(2)との間には、一定の間隙(S)(S)を形成
して、各対流ガイド板(eO)(61)上に処理水中の
固形物が滞留して腐敗するという不具合の発生を防止し
ている。
Moreover, a constant gap (S) (S) is formed between the lower end of each convection guide plate (60) +61) and the partition wall (2), and the upper end of each convection guide plate (eO) (61) is This prevents problems such as solid matter remaining in the treated water and rotting.

次に、逆洗管(15)について説明すると、同逆洗管(
15)は、好気性炉床(12)における紐状炉材(12
1))に付着した余剰汚泥を定期的に除去して、好気性
菌の活性を保持するためのものである。
Next, the backwash pipe (15) will be explained.
15) is a cord-shaped hearth material (12) in an aerobic hearth (12).
1)) Excess sludge adhering to the sludge is periodically removed to maintain the activity of aerobic bacteria.

第1図及び第4図に示すように、同逆洗管(15)は、
好気性処理室(a3)と沈澱分離室(a4)間の隔壁(
3)に沿って逆洗縦管(15b)を垂設し、その下端に
、好気性P床(12)の下方において略水平状に配設し
たエア噴出管+158)の一端を連通連結し、方、上記
した逆洗管(15b)の上端を、可撓性パイプ(15c
)を介して前記のエア配管(13c)に片持ち状態に支
持させて連通させることによって構成している。
As shown in Figures 1 and 4, the backwash pipe (15) is
Partition wall between aerobic treatment chamber (a3) and sedimentation separation chamber (a4)
3) A backwash vertical pipe (15b) is installed vertically along the backwash pipe (15b), and one end of an air jet pipe +158) arranged substantially horizontally below the aerobic P bed (12) is connected to the lower end of the backwash vertical pipe (15b), On the other hand, connect the upper end of the above-mentioned backwash pipe (15b) to the flexible pipe (15c).
), the air pipe (13c) is supported in a cantilevered manner and communicated with the air pipe (13c).

次に、好気性処理室(a3)内の処理水の一部を、嫌気
性処理室(C)の第1・室(al)に還流させる処理水
一部還流装置(E)について説明する。
Next, a treated water partial reflux device (E) for refluxing a part of the treated water in the aerobic treatment chamber (a3) to the first chamber (al) of the anaerobic treatment chamber (C) will be described.

すなわち、処理水一部還流装置(E)は、エアリフト管
(14)を、隔壁(2)に沿って垂直に配設して、一方
の散気管(13b)の上方に下端を開口させ、同上端を
処理水面(h)よりもやや上方に配設した集水桝(40
)の底面に連通させ、同集水桝(40)を隔壁(2)を
貫通した還流パイプ(70)の基端に連通させ、同パイ
プ(70)の先端を第1室(al)の上部に延設すると
共に、同先端部を下方向に屈折して処理水面(h)下で
開口させて構成している。
That is, the treated water partial recirculation device (E) has an air lift pipe (14) arranged vertically along the partition wall (2), with the lower end opening above one of the aeration pipes (13b). A water collection basin (40 mm) with the end placed slightly above the treated water level (h)
), the water collection basin (40) is connected to the base end of the return pipe (70) that penetrates the partition wall (2), and the tip of the pipe (70) is connected to the upper part of the first chamber (al). The distal end portion thereof is bent downward to open below the treated water surface (h).

そして、前記した散気管(13b)(13b)にエア配
管(13c)を介して空気を供給することにより、同散
気管(13b) (13b)より処理水中に空気を供給
し、上記エアリフト管(14)のエアリフト作用により
好気性処理室(a3)内で好気性分解処理中の処理水の
一部を集水桝(40)内に押上げると共に、同集水桝(
40)より還流パイプ(70)中を通して第1室(al
)の処理水中へ還流させて、第1室(al)における有
機物の分解処理を、嫌気性菌のみではなく、好気性処理
室からの一部還流水及びそれに作用する脱窒菌によって
も行なうことができるようにしている。
Then, by supplying air to the aeration pipes (13b) (13b) through the air piping (13c), air is supplied from the aeration pipes (13b) (13b) into the treated water, and the air lift pipe (13b) is supplied with air into the treated water. 14), a part of the treated water undergoing aerobic decomposition treatment in the aerobic treatment chamber (a3) is pushed up into the water collection basin (40), and the same water collection basin (40) is pushed up.
40) through the reflux pipe (70) into the first chamber (al
), and decomposition of organic matter in the first chamber (al) can be carried out not only by anaerobic bacteria but also by partial reflux water from the aerobic treatment chamber and denitrifying bacteria acting on it. I'm trying to make it possible.

また、嫌気性処理室(C)から好気性処理室(a3)へ
の処理水の移流量は、汚水排出管路(0)から嫌気性処
理室(C)内に流入する処理水量に一定量を増加させた
量とし、この増加景分を、処理水一部還流装置(E)に
より好気性処理室(a3)から嫌気性処理室(C)に還
流させる処理水量として、好気性処理水(a3)から後
述する沈澱分離室(a4)、消毒室(18)を経て放流
口(17)より汚水排出管路(D)の下流側へ放流する
量を、上記した汚水排出管路(D)から嫌気性処理室(
C)内へ流入する処理水量と同量にすることができる。
In addition, the transfer amount of treated water from the anaerobic treatment room (C) to the aerobic treatment room (a3) is a constant amount based on the amount of treated water flowing into the anaerobic treatment room (C) from the wastewater discharge pipe (0). The amount of aerobic treated water ( The amount discharged from a3) to the downstream side of the wastewater discharge pipe (D) from the discharge port (17) via the sedimentation separation chamber (a4) and the disinfection room (18) described later is determined by the amount discharged from the wastewater discharge pipe (D) described above. From the anaerobic treatment chamber (
The amount of treated water flowing into C) can be made equal to the amount of treated water flowing into the interior.

また、エアリフト管(14)は、第5図及び第6図に示
すように、下端開口部に空気採集傘(80)の上端(8
0b)を連通連結しており、同空気採集傘(80)は、
下端開口部(80a)を散気管(13b)の軸線方向に
幅広の拡開状に形成して、同下端開口部(8Qa )を
散気管(13t))に近接させている。
In addition, as shown in FIGS. 5 and 6, the air lift pipe (14) has an upper end (8
0b) are connected in communication, and the air collecting umbrella (80) is
The lower end opening (80a) is formed wide in the axial direction of the air diffuser pipe (13b), and the lower end opening (8Qa) is brought close to the air diffuser pipe (13t).

そして、かかる空気採集傘(80)により、散気管(1
3b)より散気される空気を確実にエアリフト管(14
)中に採集して、同エアリフト管(14)のエアリフト
作用を確実にし、上記した嫌気性処理室(C)内への処
理水の還流を円滑かつ確実にすることができるようにし
ている。
Then, by the air collecting umbrella (80), the air diffuser (1
3b) Ensure that the air diffused from the air lift pipe (14)
) to ensure the air lift action of the air lift pipe (14) and ensure smooth and reliable return of the treated water into the anaerobic treatment chamber (C).

また、第5図及び第6図中、(81)は空気採集傘(8
0)を上下摺動自在に支持する空気採集全支持ブラケッ
ト、(82)は散気管支持ブラケット、(83)はエア
樅管支持ブラケットであり、各ブラケット(81)(8
2)(83)は隔壁(2)に固設している。
In addition, in Figures 5 and 6, (81) is an air collecting umbrella (8
0) is vertically slidably supported, (82) is an aeration pipe support bracket, (83) is an air pipe support bracket, and each bracket (81) (8
2) (83) is fixed to the partition wall (2).

集水桝(40)は、本発明の要旨をなすものであり、第
7図〜第9図に示すように、上面開放の略箱形状に形成
した集水桝本体(41)と、同集水桝本体(41)の内
部を仕切る仕切板(42)とから構成している。
The water collection basin (40) constitutes the gist of the present invention, and as shown in FIGS. It consists of a partition plate (42) that partitions the inside of the water basin body (41).

そして、集水桝本体(41)は・、隔壁(2)の上部に
後方へ片持ち状態で上下スライド位置調節自在に取付け
、隔壁(2)と面接触する同集水桝本体(41)の前壁
(43)に還流パイプ(70)と連通させるための三角
せき(44)を前壁(43)の上端より切欠形成すると
共に、後壁(45)に上端より略方形状のオーバーフロ
ー開口部(46)を切欠形成している。
The water collection basin main body (41) is attached to the upper part of the bulkhead (2) in a cantilevered manner rearward so that its vertical sliding position can be adjusted freely. A triangular weir (44) for communicating with the reflux pipe (70) is cut out from the upper end of the front wall (43), and a substantially rectangular overflow opening is formed from the upper end of the rear wall (45). (46) is formed with a notch.

また、三角せき(44)は、隔壁(2)に設けた還流開
口部(2a)と符合させて、同還流開口部(2a)に−
端を連通連結した還流パイプ(70)と連通させている
。
Further, the triangular weir (44) is aligned with the reflux opening (2a) provided in the partition wall (2), and is connected to the reflux opening (2a).
It communicates with a reflux pipe (70) whose ends are connected for communication.

また、(41a)(41a)は、集水桝率#(41)の
前端左右側壁に設けた取付用耳部であり、同取付用耳部
(41a)(41a)には、それぞれ縦長のスライド用
長孔(41a)(41a)は、それぞれ縦長のスライ用
長孔(41b041b)を設け、同スライド用長孔(4
1b) (4th)中に隔壁(2)より後方へ突出させ
た取付ボルト(41c)(41c)を挿通し、同取付ボ
ルト(41c)(41c)に締付調節用ナツト(41d
)(41d)を螺着して、同締付調節用ナツト(41d
)(41d)の締付用調節により集水桝本体(41)を
隔壁(2)に沿って上下スライド調節することができる
ようにしている。
In addition, (41a) and (41a) are mounting ears provided on the left and right side walls of the front end of water collection area #(41), and the mounting ears (41a) and (41a) are provided with vertical slides, respectively. The elongated holes (41a) (41a) are each provided with a vertically elongated elongated hole (41b041b) for the slide.
1b) Insert the mounting bolts (41c) (41c) that protrude rearward from the partition wall (2) into the mounting bolts (41c) (41c), and tighten the tightening adjustment nuts (41d) into the mounting bolts (41c) (41c).
) (41d) and tighten the same tightening adjustment nut (41d).
) (41d) allows the water collection basin main body (41) to be slid up and down along the partition wall (2).

また、仕切板(42)は、集水桝本体(41)の内部に
平面視での右上りの対角線上に設けて、同集水桝本体(
41)の内部を三角せき(44)l!11とオーバーフ
ロー開口部(46)側とに仕切ると共に、同仕切板(4
2)の下部に略方形状の通水孔(42a)を開口して、
三角せき(44)側とオーバーフロー開口部(46)f
f!!Iとを同通水孔(42a)を介して連通させてい
る。
Further, the partition plate (42) is provided inside the water collection basin body (41) on a diagonal line upward to the right in plan view.
Triangular weir inside 41) (44)l! 11 and the overflow opening (46) side, and the same partition plate (4
2) a substantially rectangular water hole (42a) is opened at the bottom of the
Triangular weir (44) side and overflow opening (46) f
f! ! It communicates with I through the same water hole (42a).

このように、仕切板(42)によって、集水桝本体(4
1)内に迂回流路を形成することにより、エアリフト管
(14)の上端開口から還流パイプ(70)への直接的
な処理水の流入を防止でき、脈動を抑えて、処理水を定
常的に第1室(al)に送ることができる。
In this way, the partition plate (42) allows the water collection basin body (4
1) By forming a detour flow path inside, it is possible to prevent the treated water from directly flowing into the return pipe (70) from the upper end opening of the air lift pipe (14), suppress pulsation, and keep the treated water constant. can be sent to the first chamber (al).

また、集水桝本体(41)の底面には、オーバーフロー
開口部(46)側に位置させてエアリフト管(14)の
上部を貫通させており、上端開口部(14a)は、上記
通水孔(42a)よりも上方に位置させている。
In addition, the bottom surface of the water collection basin body (41) is located on the overflow opening (46) side, and the upper part of the air lift pipe (14) is passed through, and the upper end opening (14a) is connected to the water passage hole. (42a) is located above.

かかる構成により、好気性分解処理中の処理水の一部は
、エアリフト管(14)のエアリフト作用により同エア
リフト管(14)中を押上げられ、同エアリフト管(1
4)の上端開口部(14a)より集水桝本体(41)内
にあふれ出るようにして、気液分離している。
With this configuration, a part of the treated water during the aerobic decomposition process is pushed up in the airlift pipe (14) by the airlift action of the airlift pipe (14), and
4) Gas and liquid are separated by overflowing into the water collection basin main body (41) from the upper end opening (14a).

そして、集水桝本体(41ン内の処理水は、通水孔(4
2a)を通って三角せき(44)側に流入したものだけ
が、同三角せき(44)を越流して還流開口部(2a)
より還流パイプ(70)へ流入するようにしている。
The treated water in the water collection basin body (41 mm) is
Only the water that has flowed into the triangular weir (44) through 2a) overflows the triangular weir (44) and flows into the reflux opening (2a).
It is made to flow more into the reflux pipe (70).

この際、集水桝本体(41)のオーバーフロー開口部(
46)の開口繰下端は、還流開口部(2a)の開口縁下
端と同等若しくはそれよりも上方に位置するように、集
水桝本体(41)を上下スライド位置調節することによ
り設定し、過剰の処理水をオーバーフロー開口部(46
)より好気性処理室(a3)内に戻すことにより、還流
バイブ(70)中を通して、第1室(al)へ還流され
る処理水量を一定に保つことができるようにしている。
At this time, the overflow opening (
The lower end of the opening of 46) is set by adjusting the vertical sliding position of the water collection basin body (41) so that it is located at the same level as or above the lower end of the opening edge of the reflux opening (2a), and The overflow opening (46
) is returned to the aerobic treatment chamber (a3), so that the amount of treated water that passes through the reflux vibe (70) and is refluxed to the first chamber (al) can be kept constant.

このようにして、11M還流量を維持することにより、
嫌気性処理室TC)における嫌気性処理と好気性処理室
(a3)における好気性処理とを最適状態に維持するこ
とができるようにしている。
In this way, by maintaining the 11M reflux amount,
The anaerobic treatment in the anaerobic treatment chamber (TC) and the aerobic treatment in the aerobic treatment chamber (a3) can be maintained in optimal conditions.

また、第10図に示す(,10’)は、他の実施例とし
ての集水桝であり、仕切板(42’)の上端縁を集水模
本#(41)の上端縁高さより後方へ折返し状に伸延さ
せて、同集水桝本体(41)の上面を一部被覆する上部
カバー(42’a)を形成している。
In addition, (, 10') shown in FIG. 10 is a water collection basin as another embodiment, and the upper edge of the partition plate (42') is placed behind the upper edge height of the water collection model # (41). The upper cover (42'a) is extended in a folded manner to partially cover the upper surface of the water collection basin main body (41).

かかる上部カバー(42’a)により、エアリフト管(
14)の上端開口部(14a)より噴出した処理水が、
気液分離されないまま仕切板(42°)の上方を越えて
還流パイプ(70)中に流入するのを防止している。
This upper cover (42'a) allows the air lift pipe (
14) The treated water spouted from the upper end opening (14a),
This prevents the gas from flowing beyond the partition plate (42°) into the reflux pipe (70) without being separated into gas and liquid.

また、集水桝本体(41)の上面に、第11図に示すよ
うに、集水桝fi (47)を取付けて、同集水桝若(
47)により集水桝本体(41)の上面を閉塞すること
により、処理水がエアリフト管(14)の上端開口から
仕切板(48)の上方を越えて還流パイプ(70)へ直
接的に流入するのを防止することもできる。この場合、
仕切板(48)の高さは集水桝本体(41)の高さと時
間−とし、集水桝fi +47)による閉蓋に支障がな
いようにしている。 (48a)は通水孔である。
In addition, as shown in Fig. 11, a water collection pipe fi (47) is attached to the upper surface of the water collection pipe main body (41), and the water collection pipe waka (
47), the treated water directly flows from the upper end opening of the air lift pipe (14) over the partition plate (48) into the return pipe (70). You can also prevent it from happening. in this case,
The height of the partition plate (48) is equal to the height of the water collection basin main body (41) and the height of the water collection basin body (41), so that there is no problem in closing the lid of the water collection basin fi +47). (48a) is a water hole.

還流パイプ(70)は、第12図に示すように、第1室
(al)内に位置する第1パイプ(71)と、第2室(
a2)内に位置する第2パイプ(72)とを隔壁(1)
の上部に設けた接続パイプ(73)により接続して構成
している。
As shown in FIG. 12, the reflux pipe (70) is connected to a first pipe (71) located in the first chamber (al) and a second pipe (71) located in the first chamber (al).
a2) and the second pipe (72) located within the partition wall (1).
They are connected by a connecting pipe (73) provided at the top of the.

そして、第2パイプ(72)は、第2室(a2)内にお
いて、上記接続パイプ(73)と、前記還流開口部(2
a)との間に、第1室(al)側に下り傾斜状に連通連
結している。
The second pipe (72) connects the connection pipe (73) and the reflux opening (2) in the second chamber (a2).
a) is connected to the first chamber (al) in a downwardly inclined manner.

また、第1パイプ(71)は、第1室(al)内におい
て、接続パイプ(73)に基端に設けた雄ネジ部(71
a)を着脱自在に螺着して、第2バイズ(72)と同一
軸線方向に片持ち支持させると共に、先端部を下方へL
字状に屈曲させて、先端開口部f71b)を処理水面(
h)よりも下方に位置させている(第1図参照)。
Further, the first pipe (71) has a male threaded portion (71) provided at the base end of the connecting pipe (73) in the first chamber (al).
a) is removably screwed on and cantilevered in the same axial direction as the second vise (72), and the tip is pushed downward L.
The tip opening f71b) is bent into a letter shape so that the treated water surface (
h) (see Figure 1).

従って、好気性処理中の処理水の一部が還流させてくる
際に、空気を巻込んで第1室(al)内の処理水を過剰
に酸化するという不具合の発生を防止することができる
。
Therefore, when a part of the treated water during aerobic treatment is refluxed, it is possible to prevent the occurrence of a problem in which air is drawn in and the treated water in the first chamber (al) is excessively oxidized. .

しかも、第1バイグ(71)は、上記のように基端を接
続パイプ(73)に螺着して、同第1バイブ(71)を
軸線廻りに回転させることにより、先端開口部(71b
)の高低位置調節を行なうことができるようにしている
。
Furthermore, the first vib (71) can be opened at the tip opening (71b) by screwing the proximal end onto the connecting pipe (73) as described above and rotating the first vib (71) around the axis.
) can be adjusted in height.

従って、第1室(al)内の処理水の水位が低下して、
先端開口部171b)が処理水面(h)の上方に位置し
た場合にも、上記したように第1パイプ(71)を回転
させて先端開口部(71b)を低位置に調節することに
より、同先端開口部(71b)を処理水面(h)下に確
保することができる。
Therefore, the water level of the treated water in the first chamber (al) decreases,
Even when the tip opening 171b) is located above the treated water level (h), the same can be achieved by rotating the first pipe (71) and adjusting the tip opening (71b) to a lower position as described above. The tip opening (71b) can be secured below the treated water surface (h).

また、第1・第2パイプ(71)(72)の中途部上面
には、各パイプの軸線方向に長手状の切欠開口部(71
C)(72C)を設け、各切欠開口部(71cN72c
)より各パイプ(71)(72)内を清掃することがで
きるようにしている。
In addition, on the upper surface of the midway part of the first and second pipes (71) and (72), there is a notch opening (71) that is longitudinal in the axial direction of each pipe.
C) (72C) and each notch opening (71cN72c
) so that the inside of each pipe (71) (72) can be cleaned.

従って、各切欠開口部(71c)(72C)より第1・
第2パイプ(71)(72)内の清掃を確実に行なって
、同パイプ(71H72)の処理水還流機能を良好に確
保することができる。
Therefore, from each notch opening (71c) (72C), the first
The interior of the second pipes (71, 72) can be reliably cleaned, and the treated water recirculation function of the pipes (71H72) can be ensured well.

また、第2゛パイプ(72)の基部側には、還流処理水
層を回収して測定するための還流処理水回収部(74)
を設けている。
In addition, on the base side of the second pipe (72), there is a reflux treated water recovery section (74) for collecting and measuring the reflux treated water layer.
has been established.

すなわち、還流処理水採集部(74)は、第12図〜第
14図に示すように、第2パイプ(72)の基部側外周
面に、反転筒(75ンを上下反転自在に嵌合し、同反転
fW (75)に、第2パイプ(72)の基部側下面に
開口した流出口(72d)と符合可能に採集口(7G)
を開口し、同反転筒(75)の採集口(76)(Imの
外周面に採集ロート(77)の基端を取付け、同採集ロ
ート(77)の先端開口部(77a)を採集口(76)
と符合する位置に開口させている。
That is, as shown in FIGS. 12 to 14, the reflux treated water collecting section (74) has an inversion tube (75 tubes) fitted onto the outer peripheral surface of the base side of the second pipe (72) so as to be able to be turned upside down. , a collection port (7G) that can be aligned with the outflow port (72d) opened on the lower surface of the base side of the second pipe (72) at the same inversion fW (75).
Open the collection funnel (77), attach the proximal end of the collection funnel (77) to the outer peripheral surface of the collection port (76) (Im) of the reversing tube (75), and open the tip opening (77a) of the collection funnel (77) to the collection port (Im). 76)
The opening is made at a position that corresponds to the .

また、反転筒(75)ノ前端端部(75a)(75b)
は、第2パイプ(72)の外周面に設けた反転筒保持部
(78)(79)により水密状態で反転自在に保持させ
ている。
In addition, the front end portions (75a) (75b) of the reversing tube (75)
The second pipe (72) is held in a water-tight state so as to be freely invertable by the inverting cylinder holding parts (78) and (79) provided on the outer circumferential surface of the second pipe (72).

(79a)は防水パ・yキンである。(79a) is a waterproof jacket.

かかる構成により、反転筒(75)を先端開口部(77
a)が下方へ向くように反転させると、同先端開口部(
77a)及び採集口(78)と第2パイプ(72)の流
出口(72d)とが符合し、第2パイプ(72)中を還
流される処理水を先端開口部(77a)より採集するこ
とができる。
With this configuration, the reversing tube (75) is connected to the tip opening (77).
When a) is turned over so that it faces downward, the same tip opening (
77a) and the collection port (78) are aligned with the outlet (72d) of the second pipe (72), and the treated water flowing back through the second pipe (72) is collected from the tip opening (77a). Can be done.

従って、かかる処理水の採集量により、適量の処理水が
還流されているかどうかを簡単にチエツクすることがで
き、適量の処理水還流がなされていない場合、迅速に適
量の処理水還流がなされるように対処して、浄化槽の浄
化機能を良好に確保することができる。
Therefore, it is possible to easily check whether the appropriate amount of treated water is being refluxed by the collected amount of treated water, and if the appropriate amount of treated water is not being refluxed, the appropriate amount of treated water is quickly refluxed. By taking these measures, it is possible to ensure the purification function of the septic tank.

また、反転筒(75)を先端開口部(77a)が上方へ
向くように反転させることにより、流出口(72d)を
同反転筒(75)により閉塞して、還流処理水を第1パ
イプ(71)側へ流すことができる。
In addition, by inverting the inversion tube (75) so that the tip opening (77a) faces upward, the outlet (72d) is closed by the inversion tube (75), and the reflux treated water is transferred to the first pipe ( 71) It can flow to the side.

以上のように、好気性処理室(a3)内の構造について
説明してきたが、以下に浄化槽(^)の他の構成につい
て説明する。
As mentioned above, the structure inside the aerobic treatment chamber (a3) has been explained, but below, other structures of the septic tank (^) will be explained.

沈澱分離室(a4)は、第1図及び第3図に示すように
、隔壁(3)と消毒室(18)の隔壁(22)間とで構
成されている。
As shown in FIGS. 1 and 3, the sedimentation separation chamber (a4) is composed of a partition wall (3) and a space between the partition wall (22) of the disinfection chamber (18).

消毒室(18)は、隔壁(22)で沈澱分離室(a4)
から区画された上面開放略箱形状で一側面を浄化槽本体
(a)の側壁内面に密接させて放流口(17)と連通さ
せると共に、同消毒室(18)の上端縁(18c)を処
理水面(h)よりも僅かに低位置に設定し、また同消毒
室(18)の内側面の処理水面(h゛)よりもやや高位
置に薬剤部支持体(18a)を突設して、上方から挿入
した固形消毒薬剤充填済の薬剤1m (18b)の下端
を沈澱分離室(a4)から移流してきた処理水と接触さ
せながら支持している。
The disinfection room (18) is connected to the sedimentation separation room (a4) by the partition wall (22).
It has a box shape with an open top and one side is brought into close contact with the inner surface of the side wall of the septic tank body (a) to communicate with the discharge port (17), and the upper edge (18c) of the disinfection chamber (18) is connected to the treated water surface. (h), and a drug part support (18a) is provided protrudingly at a position slightly higher than the treated water level (h) on the inner surface of the disinfection chamber (18). The lower end of 1 m (18b) filled with a solid disinfectant inserted from the container is supported while being in contact with the treated water advected from the sedimentation separation chamber (a4).

また、(19)は、隔壁(3)から消毒室(18)の左
右両側にそれぞれ垂直に対向させて突設したスカム流出
防止板であり、同スカム流出防止板(19)は、側面を
消毒室と密接させ、上端縁を処理水面(1))上に突出
させ、下端縁を同処理水面(h)下に浸漬させて、沈澱
分離室(a4)の処理水面(h)に浮上したスカムが沈
澱分離室(a4)から消毒室(18)に移流するのを防
止している。
In addition, (19) is a scum outflow prevention plate that is vertically opposed and protrudes from the partition wall (3) on both the left and right sides of the disinfection chamber (18), and the scum outflow prevention plate (19) disinfects the sides. The scum floating on the treated water surface (h) of the sedimentation separation chamber (a4) is placed in close contact with the chamber, the upper edge protrudes above the treated water surface (1), and the lower edge is immersed below the treated water surface (h). is prevented from advecting from the sedimentation separation chamber (a4) to the disinfection chamber (18).

また、沈澱分離室(a4)と好気性処理室(a3)との
間の隔壁(3)の下端縁は、浄化槽本体(a)の内底面
と所定の間隔(n)を保持して設けられており、沈澱分
離室(a4)の内底面を、好気性処理室(a3)の方向
へ下り急傾斜させている。
Further, the lower edge of the partition wall (3) between the sedimentation separation chamber (a4) and the aerobic treatment chamber (a3) is provided with a predetermined distance (n) from the inner bottom surface of the septic tank body (a). The inner bottom surface of the sedimentation separation chamber (a4) is steeply inclined downward toward the aerobic treatment chamber (a3).

蓋体(b)は、第1図及び第2図に示すように、浄化槽
本体(a)の上端縁に固設したフランジ(a5)にボル
ト(図示せず)を介して固着されるか、又は合成樹脂に
より接着接合されて、浄化槽本体(a)の上方開口部を
閉塞しており、浄化槽本体(a)の隔壁(1)の上方位
置と、好気性処理室(a3)の上方位置とに大径の第1
、第2マンホール(bIHb2)を開閉自在に設け、薬
剤筒(18b)の上方位置に小径の第3マンホール(b
3)を開閉自在に設けている。
As shown in FIGS. 1 and 2, the lid body (b) is fixed to a flange (a5) fixed to the upper edge of the septic tank body (a) via bolts (not shown), or Or it is adhesively bonded with synthetic resin to close the upper opening of the septic tank main body (a), and the upper position of the partition wall (1) of the septic tank main body (a) and the upper position of the aerobic treatment chamber (a3). The first large diameter
, a second manhole (bIHb2) is provided so as to be openable and closable, and a small-diameter third manhole (bIHb2) is provided above the drug cylinder (18b).
3) It is provided so that it can be opened and closed freely.

以下、上記構成を有する浄化槽による、家庭の便所や厨
房からの汚水の浄化処理方法について、第1図を参照し
て説明する。
Hereinafter, a method for purifying wastewater from a household toilet or kitchen using a septic tank having the above configuration will be described with reference to FIG. 1.

汚水排出管路(D)の上流側から流入口(4)を介して
第1室(al)に流入した処理水及び同処理水中に含ま
れている有機物(水、炭水化物、蛋白質、脂質、尿素を
成分とする)は、下向流嫌気性炉床(5)を通過する間
に、同温床(5)の炉材の表面に付着した嫌気性菌によ
って嫌気分解を受ける。
The treated water flowing into the first chamber (al) from the upstream side of the sewage discharge pipe (D) through the inlet (4) and the organic matter (water, carbohydrates, proteins, lipids, urea) contained in the treated water While passing through the downward flow anaerobic hearth (5), the anaerobic bacteria (component of which are the components of

即ち、まず、酸生成菌によって処理水中の有機物を低分
子化して酢酸(CHa C0QII )やプロピオン酸
(CHa CH2Cool>等の有機酸に変え、その後
、メタン菌等の嫌気性菌によって、有機酸を分解して、
メタン(CH4)や二酸化炭素(CO2)を生成して、
これらの気体を浄化槽(八)外に放出するとともに、蛋
白質や尿素のチッソ分の分解物であるアンモニア態窒素
(NH,”−N)を含んだ処理水を生成する。
That is, first, the organic matter in the treated water is reduced in molecular weight by acid-producing bacteria and converted into organic acids such as acetic acid (CHa COQII) and propionic acid (CHa CH2Cool>), and then the organic acids are converted into organic acids by anaerobic bacteria such as methane bacteria. Take it apart and
Produces methane (CH4) and carbon dioxide (CO2),
These gases are discharged to the outside of the septic tank (8), and treated water containing ammonia nitrogen (NH, "-N), which is a decomposition product of the nitrogen component of protein and urea, is generated.

なお、下向流嫌気性炉床(5)を通過した処理水中に含
まれる組人な固形物は第1室(al)の底部に沈澱する
。
Note that the solid matter contained in the treated water that has passed through the downward flow anaerobic hearth (5) settles at the bottom of the first chamber (al).

このような嫌気性処理を行なうことによって、処理水か
ら有機物を効果的に除去することができ、その結果、嫌
気性処理後の処理水は、アンモニア態窒素(Nt14”
 −N)及び少量の未処理有機物を含んだ状態で第1室
(al)から第2室(a2)に移送されることになる。
By performing such anaerobic treatment, organic matter can be effectively removed from the treated water, and as a result, the treated water after anaerobic treatment contains ammonia nitrogen (Nt14"
-N) and a small amount of untreated organic matter is transferred from the first chamber (al) to the second chamber (a2).

即ち、嫌気性処理後の処理水は、第1稈流管(10)及
び第2移流管(11)を通過して、第2室(a2)の下
向流嫌気性炉床(9)の下方に、同沢床(9)によって
何ら嫌気性処理されることなく、直接移送される。
That is, the treated water after the anaerobic treatment passes through the first culm pipe (10) and the second advection pipe (11), and enters the downward flow anaerobic hearth (9) in the second chamber (a2). It is directly transferred downward without any anaerobic treatment by the same bed (9).

その後、下向流嫌気性炉床(9)を下から上へ通過する
間に、再び、前述したと同じ嫌気分解を受けて、さらに
、有機物の分解がなされ、その後アンモニア(8114
” −N)及びさらに少量となった未処理有機物を含ん
だ状態の処理水が、次の好気性処理室(a3)に第3移
流管(16)を介して移送される。
After that, while passing through the downward flow anaerobic hearth (9) from bottom to top, it undergoes the same anaerobic decomposition as described above, further decomposing organic matter, and then ammonia (8114
The treated water containing a further small amount of untreated organic matter is transferred to the next aerobic treatment chamber (a3) via the third advection pipe (16).

しかして、本実施例では、嫌気性処理室(C)の第2室
(a2)における嫌気性処理を、処理水を、上向流嫌気
性炉床(9)を下から上へ向けて通過する下向流とする
ことによって、嫌気性炉床を上から下に向けて通過させ
る下向流にする場合と比較して、流動速度を遅くするこ
とができ、未分解物をより多く炉床に係留させることが
でき、嫌気分解をより促進することができる。
Therefore, in this example, the anaerobic treatment in the second chamber (a2) of the anaerobic treatment chamber (C) is performed by passing the treated water through the upward flow anaerobic hearth (9) from the bottom to the top. By using a downward flow that passes through the anaerobic hearth from the top to the bottom, the flow rate can be lowered, and more undecomposed materials can be transferred to the hearth. anaerobic decomposition can be further promoted.

従って、第1室(al)における嫌気性処理と併せて、
嫌気性処理室(C)全体における嫌気性処理を効率よく
かつ充分に行なって未分解有機物の発生ないし残留を可
及的に低減することができる。
Therefore, in conjunction with the anaerobic treatment in the first chamber (al),
The anaerobic treatment in the entire anaerobic treatment chamber (C) can be performed efficiently and sufficiently to reduce the generation or residue of undecomposed organic matter as much as possible.

なお、上記嫌気性処理における酸生成菌や嫌気性菌は、
環境から処理水中に混入した酸生成菌や嫌気性菌の増殖
を待って利用することができるが、実績のある優良種菌
を接種する方が望ましい。
In addition, the acid-producing bacteria and anaerobic bacteria in the above anaerobic treatment are
Although it is possible to wait for the growth of acid-producing bacteria or anaerobic bacteria that have entered the treated water from the environment before using them, it is preferable to inoculate with a proven and excellent starter strain.

また、嫌気性処理室(C)の第1室(al)において嫌
気性処理した処理水を、第2室(a2)の底部に直接送
り、第2室(a2)の上部へ送、らないで、未分解物が
下向流嫌気性炉床(9)の上部に滞留したり、第2室(
a2)から、同第2室(a2)に並設した好気性処理室
(a3)にそのまま流入するのを確実に防止することが
できる。
In addition, the treated water that has been anaerobically treated in the first chamber (al) of the anaerobic treatment chamber (C) is sent directly to the bottom of the second chamber (a2), and is not sent to the top of the second chamber (a2). In this case, undecomposed substances may accumulate in the upper part of the downward flow anaerobic hearth (9) or in the second chamber (
a2) can be reliably prevented from directly flowing into the aerobic treatment chamber (a3) arranged in parallel with the second chamber (a2).

次に、好気性処理室(a3)内における浄化処理につい
て説明すると、好気性処理室(a3)中では、曝気装置
(13)の散気管(13b)から処理水中にエアが吹き
込まれており、同エア中の酸素を利用する硝化菌等の好
気性菌による酸化分解が行なわれて、処理水中のアンモ
ニア態窒素(Nl14”−N)は、硝酸態室(NO2−
−N)や亜硝酸態窒素<NO2−N)に酸化分解される
。
Next, the purification process in the aerobic treatment chamber (a3) will be explained. In the aerobic treatment chamber (a3), air is blown into the treated water from the aeration pipe (13b) of the aeration device (13). Oxidative decomposition is performed by aerobic bacteria such as nitrifying bacteria that utilize the oxygen in the air, and ammonia nitrogen (Nl14"-N) in the treated water is converted into a nitrate chamber (NO2-
-N) and nitrite nitrogen <NO2-N).

なお、好気性菌も、前記のように実績のある種菌を接種
する方が望ましく、好気炉床(12)は、かかる好気性
菌を付着させることで好気性菌が流出するなどによって
菌濃度が低下することがないようにしている。
In addition, it is preferable to inoculate aerobic bacteria with proven seed bacteria as described above, and the aerobic hearth (12) can be used to increase the bacterial concentration by attaching such aerobic bacteria and causing the aerobic bacteria to flow out. This is to ensure that there is no decline in

さらに、本実施例では、上記嫌気性処理及び好気性処理
を行なった処理水の全部を、そのまま浄化槽(A)外に
放流することなく、好気性処理室(a3)中で好気分解
処理中の処理水の一部(Q2)を、エアリフト管(14
)に下方から吹き込まれる散気管(13b)からのエア
により同エアリフト管(14)の上方に配設した集水桝
(40)に持ち上げ、同集水桝(40)で気液分離し、
その後、還流パイプ(70)を介して第1室(al)に
還流するようにしている。
Furthermore, in this example, all of the treated water that has been subjected to the anaerobic treatment and aerobic treatment is subjected to aerobic decomposition treatment in the aerobic treatment chamber (a3) without being directly discharged outside the septic tank (A). A part of the treated water (Q2) is transferred to the air lift pipe (14
) is lifted from below by air from a diffuser pipe (13b) into a water collection basin (40) disposed above the air lift pipe (14), and gas and liquid are separated in the water collection basin (40).
Thereafter, the water is refluxed to the first chamber (al) via the reflux pipe (70).

しかして、硝酸態窒素(NOa −−N)や亜硝酸態窒
素(NO2−−N)を含んだ処理水が第1室(al)に
流入すると、第1室(al)内に存在する脱窒菌は、こ
れら無機化合物の酸素を利用し、第1室(al)内に流
入する有機物を分解して生存のためのエネルギーを得る
。結果として、無機化合物は還元されて分子状窒素(N
2)や亜酸化窒素(N20)となり、有機物の炭素は分
解されて二酸化炭素(CO2)となり、浄化槽(A)外
に放出されることになる。
Therefore, when treated water containing nitrate nitrogen (NOa - -N) and nitrite nitrogen (NO2 - -N) flows into the first chamber (al), the desorbed water present in the first chamber (al) Nitrogen bacteria use the oxygen of these inorganic compounds to decompose organic matter flowing into the first chamber (al) to obtain energy for survival. As a result, inorganic compounds are reduced to molecular nitrogen (N
2) and nitrous oxide (N20), and the organic carbon is decomposed to become carbon dioxide (CO2), which is released outside the septic tank (A).

このように、第1室(al)における有機物の分解処理
を、嫌気性処理のみでなく、好気性処理室(a3)から
の一部還流水及びそれに作用する脱窒菌によっても行な
うことができる6 従って、嫌気性菌のみで嫌気性処理のみを行なう場合に
生じるアンモニア態窒素(Nl14 ” −N)の過剰
増加(これは嫌気性菌の活性を抑制する方向に働く)を
抑えることができ、また、かかる抑制作用によって、嫌
気性菌の活性を常時好適状態に維持することができるこ
とになり、嫌気性処理室(C)における有機物の分解処
理を飛躍的に向上することができる。
In this way, the decomposition treatment of organic matter in the first chamber (al) can be carried out not only by anaerobic treatment but also by partially refluxed water from the aerobic treatment chamber (a3) and denitrifying bacteria acting on it6. Therefore, it is possible to suppress the excessive increase in ammonia nitrogen (Nl14''-N) that occurs when performing anaerobic treatment using only anaerobic bacteria (which acts in the direction of suppressing the activity of anaerobic bacteria), and Due to this suppressing effect, the activity of the anaerobic bacteria can be maintained in a suitable state at all times, and the decomposition treatment of organic matter in the anaerobic treatment chamber (C) can be dramatically improved.

また、このような有機物の分解処理能力の向上によって
、嫌気性処理室(C)から好気性処理室(N3)に移送
する処理水中に含まれる未処理有機物も大幅に低減する
ことができ、同未処理有機物に起因する好気性処理室(
N3)内の汚泥の発生も可及的に低減することができる
。
Furthermore, by improving the ability to decompose organic matter, it is possible to significantly reduce the amount of untreated organic matter contained in the treated water transferred from the anaerobic treatment chamber (C) to the aerobic treatment chamber (N3). Aerobic treatment room due to untreated organic matter (
The generation of sludge in N3) can also be reduced as much as possible.

一方、好気性処理室(N3)における処理水中の硝酸右
窒素(NOa −−N)や亜硝酸態窒素(NO2−N)
の濃度も、処理水の一部を嫌気性処理室(C)に還流し
て、それらのイオンを脱窒菌によって分子状窒素(N2
)や亜酸化窒素(N2Q)に分解することができるので
可及的に低減することができる。
On the other hand, nitrate nitrogen (NOa--N) and nitrite nitrogen (NO2-N) in the treated water in the aerobic treatment room (N3)
The concentration of N2 is also reduced by refluxing a portion of the treated water to the anaerobic treatment chamber (C) and converting those ions into molecular nitrogen (N2) by denitrifying bacteria.
) and nitrous oxide (N2Q), so it can be reduced as much as possible.

このように、好気分解処理を終えた処理水は、隔壁(3
)の下方を迂回して沈澱分離室(N4)の下部に流入し
、処理水中に残留した極めて微量の固形物を沈澱させな
がら昇流して、消毒室(18)中に流入し、薬剤筒(1
8b)中から徐々に流出する固形消毒剤により消毒殺菌
されて、放流口(17)から処理水排出管路の下流側に
流出されることになる。
In this way, the treated water that has undergone aerobic decomposition is separated from the partition wall (3
), flows into the lower part of the sedimentation separation chamber (N4), rises while precipitating extremely small amounts of solid matter remaining in the treated water, flows into the disinfection chamber (18), and enters the chemical cylinder ( 1
8b) The treated water is disinfected and sterilized by the solid disinfectant that gradually flows out from inside, and is then discharged from the outlet (17) to the downstream side of the treated water discharge pipe.

なお、沈澱分離室(N4)を昇流型としたことで、スラ
ッジブラケットが生成し、比較的軽比重かつ小さなフロ
ックまで捕集することができ、更に同沈澱分離室(N4
)の内底面を好気性処理室(N3)の方向へ下り急傾斜
させたことで、同沈澱分離室(N4)中の沈澱汚泥は好
気性処理室(N3)の底部に移動させるようにしている
。
In addition, by making the sedimentation separation chamber (N4) a riser type, sludge brackets are generated and even relatively light specific gravity and small flocs can be collected.
) is steeply sloped downward in the direction of the aerobic treatment chamber (N3), so that the settled sludge in the sedimentation separation chamber (N4) is moved to the bottom of the aerobic treatment chamber (N3). There is.

このようにして、家庭の便所や厨房等からの処理水を浄
化処理して処理水排水管路の下流側に放流した最終処理
水は、前述したように、好気性処理室(N3)中の処理
水の一部を還流する構成としているので、ROD濃度や
窒素濃度を著しく低減できる。
In this way, the final treated water that is purified from the domestic toilets, kitchens, etc. and discharged to the downstream side of the treated water drainage pipe is stored in the aerobic treatment room (N3). Since a part of the treated water is refluxed, the ROD concentration and nitrogen concentration can be significantly reduced.

本出願人が行った実験によれば、本実施例に係る浄化槽
(^)によって得られた最終処理水中におけるBOD濃
度等は、以下の表に示す通りであった。
According to experiments conducted by the present applicant, the BOD concentration etc. in the final treated water obtained by the septic tank (^) according to this example were as shown in the table below.

なお、数値は平均値表現である。Note that the numerical values are expressed as average values.

単位(II(1/J ) 以上の表からも明らかなように、本実施例の場合、従来
の浄化槽と比較してBOD濃度等を著しく低減すること
ができる。
Unit (II (1/J)) As is clear from the above table, in the case of this example, the BOD concentration etc. can be significantly reduced compared to the conventional septic tank.

また、嫌気性処理室(C)に流入する処理水の量を(0
1)、好気性処理室(N3)から嫌気性処理室tc)へ
の一部還流量を(N2)とすれば、嫌気性処理室(C)
から好気性処理室(N3)に移送される処理水の量(N
3)は、Q3= Q1十02となるが、Ql:Q2=1
:1〜10(i適には1:2〜6)とするのが好ましい
ことがわかった。
In addition, the amount of treated water flowing into the anaerobic treatment chamber (C) is (0
1) If the partial recirculation amount from the aerobic treatment chamber (N3) to the anaerobic treatment chamber tc) is (N2), then the anaerobic treatment chamber (C)
The amount of treated water (N
3) becomes Q3=Q1102, but Ql:Q2=1
:1 to 10 (suitably 1:2 to 6).

ところで、当初の流入処理水中には、例えば合成繊維細
片、砂粒、合成樹脂フィルム細片等の非分解性固形物が
混入することがあるため、どうしても、浄化槽(a)の
各室、即ち、第1室(al)、第2室(N2)、好気性
処理室(N3)中に分解しきれない固形物ないし剥離菌
の遺骸からなる汚泥が堆積する。
By the way, since non-degradable solids such as synthetic fiber fragments, sand grains, and synthetic resin film fragments may be mixed in the initial inflow treated water, it is inevitable that each chamber of the septic tank (a), i.e., Sludge consisting of undecomposed solid matter or the remains of exfoliated bacteria accumulates in the first chamber (al), the second chamber (N2), and the aerobic treatment chamber (N3).

この場合は、蓋体(b)の第1、第2マンホール(bl
)(b2)を開き、第1、第2移流管(10)(11)
を通路とすることで、第1室(al)と第2室(N2)
の底部に固形物や汚泥を吸い取るためのバキュームホー
スを容易に挿入することができ、また、好気性処理室(
N3)中の固形物や汚泥を吸い取ることで、沈澱分離室
(N4)の固形物も同時に吸い収られる。また、第3マ
ンホール(b3)を開いて、薬剤筒(18b)の取り替
えを楽に行なうことができる。
In this case, the first and second manholes (bl
) (b2), and open the first and second advection tubes (10) (11).
By using the passage as a passage, the first chamber (al) and the second chamber (N2)
A vacuum hose can be easily inserted into the bottom of the chamber to suck up solids and sludge, and an aerobic treatment chamber (
By sucking up the solids and sludge in N3), the solids in the sedimentation separation chamber (N4) are also sucked up at the same time. Furthermore, the third manhole (b3) can be opened to easily replace the medicine cartridge (18b).

また、好気性P床(12)には、余剰汚泥が付着するが
、三方ボールバルブ(55)を操作して、逆洗管(15
)の噴出管(15a)から空気を噴出させるとともに、
可撓性バイブ(15C)を介して、噴出管(15a)を
手動により揺動させることで、上記余剰汚泥を確実に洗
い落とすことができる。
In addition, surplus sludge adheres to the aerobic P bed (12), but by operating the three-way ball valve (55), the backwash pipe (15)
) and eject air from the ejection pipe (15a),
By manually swinging the ejection pipe (15a) via the flexible vibrator (15C), the excess sludge can be reliably washed away.

(へ)効果 本発明によれば、以下のような効果が生起される。(to) Effect According to the present invention, the following effects are produced.

■本発明では、好気性処理を行なった処理水の一部を嫌
気性処理室に還流して、嫌気性処理室における有機物の
分解処理を、嫌気性菌のみでなく、好気性処理室からの
一部還流水及びそれに作用する脱窒菌によっても行なう
ことができる。従って、嫌気性菌のみで嫌気性処理のみ
を行なう場合に生じるアンモニア(NH4)の過剰増加
(これは嫌気性菌の活性をRMする方向に働く)を抑え
ることができ、また、かかる抑制作用によって、嫌気性
菌の活性を常時好適状態に維持することができることに
なり、嫌気性処理室における有機物の分解処理を飛躍的
に向上することができる。
■In the present invention, a part of the treated water that has undergone aerobic treatment is returned to the anaerobic treatment chamber, and the decomposition of organic matter in the anaerobic treatment chamber is performed not only by anaerobic bacteria but also by the aerobic treatment chamber. It can also be carried out using partially refluxed water and denitrifying bacteria acting on it. Therefore, it is possible to suppress the excessive increase in ammonia (NH4) that occurs when performing anaerobic treatment only with anaerobic bacteria (which acts in the direction of RM the activity of anaerobic bacteria), and due to this suppressive effect, Therefore, the activity of the anaerobic bacteria can be maintained in a suitable state at all times, and the decomposition treatment of organic matter in the anaerobic treatment chamber can be dramatically improved.

■このような有機物の分解処理能力の向上によって、嫌
気性処理室から好気性処理に移送する処理水中に含まれ
る未処理有機物も大幅に低減することができ、同未処理
有機物に起因する好気性処理室内の汚泥の発生も可及的
に防止することができる。
■By improving the ability to decompose organic matter, the untreated organic matter contained in the treated water transferred from the anaerobic treatment room to the aerobic treatment room can be significantly reduced, and the aerobic The generation of sludge in the treatment chamber can also be prevented as much as possible.

■有機物の分解処理能力の向上によって、浄化槽のコン
パクト化を図ることもできる。
■By improving the ability to decompose organic matter, it is possible to make septic tanks more compact.

■上記したような処理水の一部還流によって、最終処理
水のBOD濃度や窒素濃度を著しく低減でき、浄化能力
の向上を図ることができる。
(2) By partially refluxing the treated water as described above, the BOD concentration and nitrogen concentration of the final treated water can be significantly reduced, and the purification ability can be improved.

■集水桝には、オーバーフロー開口部を設けて、過剰な
処理水が嫌気性処理室に還流されるのを防止して、還流
量を一定に確保しているために、上記した嫌気性菌の活
性の抑制防止と窒素除去能力の向上を確実に図ることが
できる。
■The water collection basin has an overflow opening to prevent excess treated water from flowing back into the anaerobic treatment chamber and to ensure a constant flow of water, the anaerobic bacteria mentioned above It is possible to reliably prevent inhibition of the activity of nitrogen and improve the nitrogen removal ability.

■処理水を一旦集水桝に集めた後に嫌気性処理室へ還流
するようにしているなめに、集水桝内で処理水の気液分
離を確実に行なうことができて、空気を取込んだ溶存酸
素量の多い処理水により嫌気性処理室内の嫌気性菌の活
性を抑制するという不具合の発生を防止することができ
る。
■Because the treated water is collected in the catch basin and then returned to the anaerobic treatment room, it is possible to reliably separate gas and liquid from the treated water in the catch basin, and to take in air. However, it is possible to prevent the occurrence of a problem in which the activity of anaerobic bacteria in the anaerobic treatment chamber is suppressed by treated water with a large amount of dissolved oxygen.

■処理水をエアリフト管のエアリフト作用により集水桝
内に押上げるようにしているために、別途処理水押上げ
用のポンプ等の駆動源を設ける必要がなく、浄化槽の構
造を簡単にすることができ、製造コストの低減化を図る
ことができる。
■Since the treated water is pushed up into the water collection basin by the air lift action of the air lift pipe, there is no need to separately provide a drive source such as a pump for pushing up the treated water, simplifying the structure of the septic tank. This makes it possible to reduce manufacturing costs.

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

第1図は、本発明による集水桝構造を具備する浄化槽の
断面側面図。 第2図は、第1図のI−I線断面図。 第3図は、浄化槽本体の平面図。 第4図は、好気性処理室の平面図。 第5図は、好気性処理室内の一部正面図。 第6図は、空気採集傘の平面図。 第7図は、集水桝の平面図。 第8図は、集水桝の正面図。 第9図は、集水桝の一部切欠拡大斜視図。 第10図は、他の実施例としての集水桝の斜視図。 第11図は、もう一つの他の実施例としての集水桝の斜
視図。 第12図は、還流パイプの拡大側面図。 第13図は、還流処理水採集部の一部切欠拡大側面図。 第14図は、第13図の■−■線断面図。 第15図は、従来の浄化槽の断面図。 (^) FC) (al) (a2) (a3) (a4) 浄化槽 嫌気性処理室 第1室 第2室 好気性処理室 沈澱分離室 隔壁 第1移流管 第2移流管 エアリフト管 消毒室 集水桝 還流パイプ
FIG. 1 is a cross-sectional side view of a septic tank equipped with a water collection basin structure according to the present invention. FIG. 2 is a sectional view taken along the line II in FIG. 1. FIG. 3 is a plan view of the septic tank body. FIG. 4 is a plan view of the aerobic treatment chamber. FIG. 5 is a partial front view of the inside of the aerobic treatment chamber. FIG. 6 is a plan view of the air collection umbrella. Figure 7 is a plan view of the water collection basin. Figure 8 is a front view of the water collection basin. FIG. 9 is a partially cutaway enlarged perspective view of the water collection basin. FIG. 10 is a perspective view of a water collection basin as another embodiment. FIG. 11 is a perspective view of a water collection basin as another embodiment. FIG. 12 is an enlarged side view of the reflux pipe. FIG. 13 is a partially cutaway enlarged side view of the reflux treated water collection section. FIG. 14 is a sectional view taken along the line ■-■ in FIG. 13. FIG. 15 is a sectional view of a conventional septic tank. (^) FC) (al) (a2) (a3) (a4) Septic tank Anaerobic treatment room 1st room 2nd room Aerobic treatment room Sedimentation separation room Partition wall 1st advection pipe 2nd advection pipe Air lift pipe Disinfection room Water collection Basin reflux pipe

Claims (1)

【特許請求の範囲】 1)好気性処理室(a3)内の下部に散気管(13b)
を配設し、同散気管(13b)の上方にエアリフト管(
14)の下端を開口すると共に、同エアリフト管(14
)の上端を集水桝(40)を介して嫌気性処理室(C)
内と連通させ、散気管(13b)にエア配管(13c)
を介して空気を供給することにより、同散気管(13b
)より処理水中に空気を供給し、上記エアリフト管(1
4)のエアリフト作用により好気性処理室(a3)内で
好気性分解処理中の処理水の一部を、集水桝(40)内
に押上げると共に、同集水桝(40)より一定量だけ連
続して嫌気性処理室(C)に還流させるように構成した
浄化槽における集水桝構造。 2)請求項1記載の集水桝(40)を略箱形状に形成し
、同集水桝(40)の一側壁に嫌気性処理室(C)と連
通する連通口を開口すると共に、同集水桝(40)の他
側壁にオーバーフロー開口部(46)を切欠形成し、か
つ集水桝(40)の底面よりオーバーフロー開口部(4
6)の下端縁までの高さを、集水桝(40)の底面より
連通口の下端縁までの高さよりも高くして、集水桝(4
0)の底面に連通連結したエアリフト管(14)中を通
して集水桝(40)内に押上げられてくる好気性分解処
理中の処理水の一部を一定量だけ連通口を通して嫌気性
処理室(C)へ還流可能としてなる浄化槽における集水
桝構造。
[Claims] 1) A diffuser pipe (13b) in the lower part of the aerobic treatment chamber (a3)
An air lift pipe (
The lower end of the air lift pipe (14) is opened, and the lower end of the air lift pipe (14) is opened.
) to the anaerobic treatment chamber (C) via the water collection basin (40).
Connect the air pipe (13c) to the air diffuser pipe (13b).
By supplying air through the air diffuser pipe (13b
) from the air lift pipe (1).
Due to the air lift effect of 4), a part of the treated water undergoing aerobic decomposition treatment in the aerobic treatment chamber (a3) is pushed up into the water collection basin (40), and a certain amount is also lifted from the collection water basin (40). A water collection basin structure in a septic tank configured to allow water to continuously flow back to the anaerobic treatment chamber (C). 2) The water collection basin (40) according to claim 1 is formed into a substantially box shape, and a communication port communicating with the anaerobic treatment chamber (C) is opened in one side wall of the water collection basin (40). An overflow opening (46) is cut out in the other side wall of the water collection basin (40), and the overflow opening (46) is cut out from the bottom of the water collection basin (40).
6) The height to the lower edge of the water collection basin (40) is set higher than the height from the bottom of the water collection basin (40) to the lower edge of the communication port.
A certain amount of the treated water during the aerobic decomposition process is pushed up into the water collection basin (40) through the air lift pipe (14) connected to the bottom of the anaerobic treatment chamber through the communication port. A water collection basin structure in a septic tank that allows water to flow back to (C).
JP4394589A 1989-02-25 1989-02-25 Structure of collecting inlet chamber of septic tank Pending JPH02222780A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4394589A JPH02222780A (en) 1989-02-25 1989-02-25 Structure of collecting inlet chamber of septic tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4394589A JPH02222780A (en) 1989-02-25 1989-02-25 Structure of collecting inlet chamber of septic tank

Publications (1)

Publication Number Publication Date
JPH02222780A true JPH02222780A (en) 1990-09-05

Family

ID=12677841

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4394589A Pending JPH02222780A (en) 1989-02-25 1989-02-25 Structure of collecting inlet chamber of septic tank

Country Status (1)

Country Link
JP (1) JPH02222780A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100303939B1 (en) * 1999-07-03 2001-09-24 배동엽 A Sequential Batch Reactor type tank, which use cubic type floating material containing elvan and ativated carbon for purifying sewage
JP2012213698A (en) * 2011-03-31 2012-11-08 Kubota Corp Sewage purification facility
JP2013158758A (en) * 2012-02-08 2013-08-19 Panasonic Corp Gas dissolution device

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100303939B1 (en) * 1999-07-03 2001-09-24 배동엽 A Sequential Batch Reactor type tank, which use cubic type floating material containing elvan and ativated carbon for purifying sewage
JP2012213698A (en) * 2011-03-31 2012-11-08 Kubota Corp Sewage purification facility
JP2013158758A (en) * 2012-02-08 2013-08-19 Panasonic Corp Gas dissolution device

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