JPH02222778A - Baffle plate structure for septic tank - Google Patents

Baffle plate structure for septic tank

Info

Publication number
JPH02222778A
JPH02222778A JP4395189A JP4395189A JPH02222778A JP H02222778 A JPH02222778 A JP H02222778A JP 4395189 A JP4395189 A JP 4395189A JP 4395189 A JP4395189 A JP 4395189A JP H02222778 A JPH02222778 A JP H02222778A
Authority
JP
Japan
Prior art keywords
chamber
septic tank
baffle plate
sewage
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
JP4395189A
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 JP4395189A priority Critical patent/JPH02222778A/en
Publication of JPH02222778A publication Critical patent/JPH02222778A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To improve an anaerobic treatment capacity by disposing a baffle plate right below an inflow port in the state of accepting the inflow sewage from the inflow port, once receiving the sewage by this baffle plate and allowing the sewage to flow downward to a purifying section. CONSTITUTION:The baffle plate 25 is formed to a rectangular shape broader than the aperture diameter of the inflow port 4 and is mounted to the front end of a baffle plate stay 26 extended from the front wall of a septic tank body to just below the inflow port 4. The side of the front end edge 25a of the plate 25 is positioned in proximity to the inflow port 4 and the rear end edge 25b side is inclined to be high on the front and low in the rear near the center of the 1st chamber (a1) and in proximity to the surface (h) side of the water to be treated. The water to be treated flowing into the 1st chamber (a1) from the inflow port 4 is dropped onto a downward current anaerobic filter bed 5 along the plate 25 in this way and, therefore, the water to be treated is prevented from passing linearly in the filter bed 5. The anaerobic treatment of the water to be treated by the filter bed 5 is surely executed and the solids in the inflow water to be treated are dispersed by the plate 25. The anaerobic treatment efficiency is thus well assured. The destruction of the scum layer formed on the surface (h) of the water to be treated is prevented.

Description

【発明の詳細な説明】 (イ) 産業上の利用分野 本発明は、浄化槽における邪魔板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 baffle structure in a septic tank.

(ロ) 従来の技術 従来、浄化槽の一形態として、浄化槽本体の一側に、汚
水排出管路の上流側と連通ずる流入口を設けると共に、
同浄化槽本体のfll!!側に、汚水排出管路の下流側
と連通ずる放流口を設け、上記流入口より浄化槽本体内
に流入する汚水を、同浄化槽本体に設けた浄化処理部に
より杼化処理して放流口より下水管路の下流側へ放流す
べく構成したものがある。
(b) Conventional technology Conventionally, as a form of septic tank, an inlet is provided on one side of the septic tank body to communicate with the upstream side of the sewage discharge pipe.
Full of the same septic tank body! ! A discharge port is provided on the side that communicates with the downstream side of the sewage discharge pipe, and the sewage that flows into the septic tank body from the inlet is processed into a shed by the septic processing unit installed in the septic tank body, and is then drained from the discharge port. Some are configured to discharge water downstream of the water pipe.

(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、以下のような問題点があ
った。
(c) Problems to be Solved by the Invention However, in the case of the above-mentioned septic tank, there were the following problems.

■浄化槽本体内に大量の汚水が直線的に流入し、浄化処
理部中をそのまま通過して浄化処理が全く行なわれない
虞があった。
■There was a risk that a large amount of sewage would flow straight into the septic tank body, pass through the purification treatment section, and no purification treatment would be carried out at all.

■浄化槽本体内に汚水が直線的に流入する際に、浄化処
理部に空気を巻込む虞があり、同浄化処理部にて嫌気性
処理を行なう場合には、かかる空気の巻込み混入により
汚水中の溶存酸素量が増大し、嫌気性菌の活性を抑制す
るという問題があった。
■When sewage flows straight into the septic tank body, there is a risk of air being drawn into the septic tank, and when anaerobic treatment is performed in the septic tank, the sewage may be mixed in with such air. There was a problem in that the amount of dissolved oxygen inside increased, suppressing the activity of anaerobic bacteria.

■直線的に流入する汚水が、浄化槽本体内の汚水面に形
成されているスカム層を破壊し、同スカム層により維持
されていた空気接触防止機能が果されなくなり、嫌気性
処理能力が低下するという問題があった。
■The sewage flowing in a straight line destroys the scum layer formed on the sewage surface inside the septic tank, and the scum layer no longer functions to prevent air contact, reducing the anaerobic treatment capacity. There was a problem.

■直線的に流入する汚水が、浄化槽本体内に溜っている
汚水に衝突して騒音を生じるという問題があった。
■There was a problem in that the sewage flowing in a straight line collided with the sewage accumulated inside the septic tank body, causing noise.

(ニ) 課題を解決するための手段 そこで、本発明では、浄化槽本体の一側に、汚水排出管
路の上流側と連通ずる流入口を設けると共に、同浄化槽
本体の他側に、汚水排出管路の下流側と連通ずる放流口
を設け、上記流入口より浄化槽本体内に流入する汚水を
、同浄化槽本体に設けた浄化処理部により浄化処理して
放流口より汚水排出管路の下流側へ放流すべく構成した
浄化槽において、流入口の直下方に、流入口からの流入
汚水を受止める状態で邪魔板を配設し、同邪魔板で一旦
汚水を受止めて浄化処理部へ流下させるべく構成してな
る浄化槽における邪魔板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 inlet communicating with the upstream side of the sewage discharge pipe is provided on one side of the septic tank body, and a sewage discharge pipe is provided on the other side of the septic tank body. A discharge port is provided that communicates with the downstream side of the septic tank, and the sewage flowing into the septic tank body from the inlet is purified by a purification processing unit provided in the septic tank body, and then flows from the discharge port to the downstream side of the sewage discharge pipe. In a septic tank configured to discharge water, a baffle plate is placed directly below the inlet to catch the inflowing sewage from the inlet, and the baffle plate is used to temporarily catch the sewage and allow it to flow down to the purification treatment section. The present invention aims to provide a baffle plate structure for a septic tank constructed by the present invention.

また、邪魔板を、放流口側に向けて前低後高に傾斜させ
たことにも特徴を有する。
Another feature is that the baffle plate is inclined toward the outlet side with a lower front and rear height.

(ポ) 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(A)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。
(Po) Embodiment The embodiment of the present invention will be explained in detail based on the drawings. In Figs. 1 and 2, (A) shows a household septic tank, and the septic tank (A) is a septic tank main 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
部を第1室(al)、第2室(a2)、好気性処理室(
a3)、沈澱分離室(a4)、消毒室(18)の5室に
分割し、第1室(al)と第2室(a2)で嫌気性処理
室(C)を構成している。
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 with partition walls (1), (2), and (3).
The interior is divided into a first chamber (al), a second chamber (a2), and an aerobic treatment chamber (
It is divided into five rooms: a3), a sedimentation separation room (a4), and a disinfection room (18), and the first room (al) and the second room (a2) constitute an anaerobic treatment room (C).

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
丁字形状で汚水排出管路(D)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) is approximately horizontally shaped and communicates with the upstream side of the sewage discharge pipe (D). ) The sewage water (hereinafter referred to as "treated water") flowing into the first chamber (al) is guided downward in a curved manner.

また、上記流入口(4)の直下方には、流入口(4)か
らの流入汚水を受止める状態で邪魔板(25)を配設し
、同邪魔板(25)で一旦汚水を受止めて浄化処理部と
しての第1室(al)内へ流下させるようにしている。
In addition, a baffle plate (25) is provided directly below the inlet (4) to catch the wastewater flowing in from the inlet (4), and the baffle plate (25) temporarily catches the wastewater. It is made to flow down into the first chamber (al) serving as a purification processing section.

かかる邪魔板(25)は、本発明の要旨をなすものであ
り、以下第1図、第3図及び第4図にもとづき説明する
This baffle plate (25) constitutes the gist of the present invention, and will be explained below based on FIGS. 1, 3, and 4.

すなわち、邪魔板(25)は、流入口(4)の開口径よ
りも広幅の矩形状に形成して、浄化槽本体(a)の前壁
(21)より流入口(4)の直下方まで伸延させた邪魔
板ステー(26)の先端に取付けている。
That is, the baffle plate (25) is formed into a rectangular shape wider than the opening diameter of the inlet (4), and extends from the front wall (21) of the septic tank body (a) to just below the inlet (4). It is attached to the tip of the baffle plate stay (26).

そして、邪魔板(25)は、前端縁(25a)側を流入
口(4)に近接させると共に、後端縁(25b) IP
!を第1室(al)の中心寄りでかつ処理水面(h)側
に近接させた前高後低の傾斜状としている。
The baffle plate (25) has a front edge (25a) close to the inlet (4), and a rear edge (25b)
! is inclined toward the center of the first chamber (al) and close to the treated water surface (h) with a high front and a low rear.

このように、邪魔板(25)を流入口(4)の直下方に
配設しているなめに、以下のような作用効果が生起され
る。
As described above, since the baffle plate (25) is disposed directly below the inlet (4), the following effects are produced.

すなわち、流入r:I(4)より第1室(al)内に流
入してくる処理水を、邪魔板(25)に沿って後述する
下向流嫌気性炉床(5)上に落下させることができるた
めに、処理水が下向流嫌気性炉床(5)中を直線的に通
過するのを防止することができ、同下向流嫌気性炉床(
5)による処理水の嫌気性処理を確実に行なわせること
ができる。特に、流入処理水中の固形物を邪魔板(25
)により分散させて、嫌気性処理能率を良好に確保する
ことができる。
That is, the treated water flowing into the first chamber (al) from the inflow r:I (4) is caused to fall onto the downward flow anaerobic hearth (5), which will be described later, along the baffle plate (25). As a result, it is possible to prevent the treated water from passing straight through the downward flow anaerobic hearth (5).
The anaerobic treatment of the treated water according to 5) can be reliably performed. In particular, baffle plates (25
) to ensure good anaerobic treatment efficiency.

しかも、処理水が直線的に流入することによる第1室(
al)内の処理水への空気の巻込みを防止することがで
きるために、同処理水中の溶存酸素量が増大して嫌気性
菌の活性が抑制される′という不具合の発生を防止する
ことができる。
Moreover, the first chamber (
al) to prevent the occurrence of problems such as the amount of dissolved oxygen in the treated water increasing and the activity of anaerobic bacteria being suppressed by preventing air from being entrained in the treated water; Can be done.

さらに、第1室(al)内の処理水面(h)に形成され
たスカム槽が、直線的に流入する処理水によって破壊さ
れるという不具合の発生を防止することができ、同スカ
ム層による第1室(al)内の処理水と空気との接触防
止を良好に確保して、同第1室(al)内における嫌気
性処理能力を良好に確保することができる。
Furthermore, it is possible to prevent the occurrence of a problem in which the scum tank formed on the treated water surface (h) in the first chamber (al) is destroyed by the treated water flowing linearly. It is possible to satisfactorily ensure that the treated water in the first chamber (al) is prevented from coming into contact with air, and to satisfactorily ensure the anaerobic treatment capacity in the first chamber (al).

また、処理水落下時に、同処理水が第1室(al)内に
溜っている処理水に直接衝突することがなくなるために
、騒音の発生を防止することができる。
Moreover, since the treated water does not directly collide with the treated water accumulated in the first chamber (al) when it falls, it is possible to prevent the generation of noise.

以下に、浄化槽(A)の他の構成について説明する。Other configurations of the septic tank (A) will be described below.

また、第1室(al)中には、流入口(4)から下方向
に所定間隔を設けて下向流嫌気性P床(5)を設けてお
り、同上向流嫌気性枦床(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°)間に炉材を充
填して構成している。
Further, in the first chamber (al), a downward flow anaerobic P bed (5) is provided at a predetermined interval downward from the inlet (4), and an upward flow anaerobic P bed (5) is provided in the first chamber (al). ) 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
The furnace material is filled between the upper and lower furnace material shelves (7) (7 degrees).

炉材は、表面積及び空隙率を著しく高めるように形成さ
れた合成樹脂やその他の素材からなる。
Furnace materials are made of synthetic resin or other materials shaped to significantly increase surface area and porosity.

第2室(a2)は、内部に上向流嫌気性枦床(9)を収
容しており、前記の下向流嫌気性炉床(5)と略同−構
造であるが、r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r床(5)と異なる。 (8
)(8°)は上下部炉材棚、(8a)(8b)は支持体
である。
The second chamber (a2) houses an upward flow anaerobic hearth (9), and has approximately the same structure as the above-mentioned downward flow anaerobic hearth (5). This differs from the r-bed (5) in that the porosity is smaller and the surface area is larger. (8
) (8°) are upper and lower furnace material 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)側と第2室(a2)側の側面に沿って立設した第1
・第2移流管(10)(11)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)
1) side and the 2nd chamber (a2) side.
・Performed through the second advection tubes (10) and (11).

第1・第2移流管(10)(11)は、第3図に示すよ
うに、それぞれ断面時■4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壁(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r床(5)(9)の上下方で開放した
管体を形成し、各移流管(10)(11)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.
Place one edge of each partition wall (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 r floor (5) and (9), respectively. A partition wall (1) between each advection tube (10) (11)
), a substantially square-shaped communication port (21) reaching a position slightly lower than the treated water level (h) from above is cut out to form the first chamber (al).
and the second chamber (a2) are communicated with each other.

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 #Jl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(3
0)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 2 #Jl are arranged, and the first room (
There are also a pair of left and right communication ports (21) that communicate between the communication ports (21) and the second chamber (a2), and each communication port (21) has a movable weir (3).
0) is installed so that it can be slid up and down.

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S!(1)に近接する浄化
槽本体(a)の側壁(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).
It is formed into a serrated shape, and the distance is S! Guide rails (31) (31°) provided on the inner surface of the side wall (20) of the septic tank body (a) adjacent to (1) and on the inner surface of the side wall of the second advection pipe (11) facing the same inner surface. It is fitted in so that it can slide up and down freely.

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、同摺動涌(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。
Furthermore, an adjustment bolt sliding groove (32) is formed vertically in the center of the movable weir (30) from the lower end to the center, and the adjustment bolt slides through the sliding groove (32) and attaches 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.

好気性処理室(a3)は、第1図、第3図及び第5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。
As shown in FIGS. 1, 3, and 5, 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.

好気性P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(12b)を多数支持させて構成している。
The aerobic P bed (12) has a frame (12a) sunk in the aerobic treatment chamber (a3) at a predetermined distance from the inner bottom surface, and a large number of fibrous strings attached to the center string in a substantially tufted shape. It is constructed by supporting a large number of string-like swamp members (12b) formed by

また、好気性r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, as a furnace material for an aerobic r-bed, the present invention uses string-like 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孔状の散気管(1
3b) (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(13c)を介して供給
される空気を処理水中に散気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)
a) Porous air diffusers (1
3b) (13b) are connected in a substantially horizontal manner so that the air supplied to the upper end of the vertical air pipe (13a) via the air pipe (13c) is diffused into the treated water.

そして、エア配管(13c)の中途部には、散気管(1
3b)に供給するエア量を調節するためのエア量調節部
(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 the middle of the air pipe (13c), there is a diffuser pipe (1
3b), and a three-way ball valve (50) for switching and supplying the air supplied to the diffuser pipe (13b) to the backwash pipe (15), which will be described later. 55).

また、左右の散気管(1311)(13b)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(6
0)(61)を配設しており、各対流ガイド板(60)
(61)は、下端部を隔壁(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。
In addition, convection guide plates (6
0) (61) are arranged, and each convection guide plate (60)
(61) is a supporting member whose lower end is attached to the partition wall (2)! 62)(
63), and the midway portion is curved upward in a convex manner to bring the upper end close to the treated water surface (h).

しかも、各対流ガイトイ板(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(60)(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 each convection guide plate (60) (61) This prevents problems such as solid matter in the treated water remaining on top and rotting.

エアリフト管(14)は、隔壁(2)に沿って垂直に配
設されており、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(14a)の底面を貫通させて同底面のや
や上方で開口させており、同集水桝(14a)を隔壁(
2)を貫通した返送パイプ(14b)の一端に連通させ
、同パイプ(14b)の他端を第1室(1a)の上部に
延設すると共に、同他端先端部を下方向に屈折して処理
水面(h)下で開口させている。
The air lift pipe (14) is arranged vertically along the partition wall (2), with its lower end opening above one of the diffuser pipes (13b), and its upper end slightly above the treated water level (h). The bottom of the installed water collection basin (14a) is penetrated and opened slightly above the bottom, and the water collection basin (14a) is connected to the partition wall (
2), the other end of the return pipe (14b) is extended to the upper part of the first chamber (1a), and the tip of the other end is bent downward. It is opened below the treated water surface (h).

また、第2室(a2)の上方に位置する返送パイプ(1
4b)の中途部には、パイプ内清掃用の切欠開口部(1
4f)と、返送処理水量を測定するための返送処理水採
集部(40)をそれぞれ設けている。
In addition, the return pipe (1) located above the second chamber (a2)
In the middle part of 4b), there is a notch opening (1) for cleaning inside the pipe.
4f) and a return treated water collection section (40) for measuring the amount of returned treated water.

集水桝(14a)は、第6図に示すように、上面開放の
略箱形状に形成して、隔壁(2)の上部に片持ち状態で
上下スライド位置調節自在に取付けており、内部には平
面視での右上りの対角線上に仕切板(14c)を設けて
、同仕切板(14c)の下部に略方形状の通水孔(14
d)を開口し、同仕切板(14c)の一側にエアリフト
管(14)の上端を開口させ、他側を返送パイプ(14
b)と連通させている。
As shown in Fig. 6, the water collection basin (14a) is formed into a box shape with an open top, and is attached to the top of the bulkhead (2) in a cantilevered manner so that its vertical sliding position can be adjusted. A partition plate (14c) is provided on the diagonal line on the upper right side in plan view, and a substantially rectangular water passage hole (14c) is provided at the bottom of the partition plate (14c).
d), the upper end of the air lift pipe (14) is opened on one side of the partition plate (14c), and the return pipe (14) is opened on the other side.
b).

このように、仕切板(14C)によって、集水桝(14
a)に迂回流路を形成して、エアリフト管(14)の上
端開口から返送パイプ(14b)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 water collection basin (14C) is separated by the partition plate (14C).
By forming a bypass flow path in a), it is possible to prevent the treated water from directly flowing into the return pipe (14b) from the upper end opening of the air lift pipe (14), suppress pulsation, and constantly supply the treated water. 1
It can be sent to the room (al).

また、集水桝(14a)の一側面には、上方から略方形
状のオーバーフロー開口部(14c)を切欠形成すると
共に、他側面には、返送パイプ(14b)と連通させる
ための三角せき(14(1)を切欠形成している。
In addition, a substantially rectangular overflow opening (14c) is cut out from above on one side of the water collection basin (14a), and a triangular weir (14c) for communicating with the return pipe (14b) is formed on the other side. 14(1) is formed with a notch.

そして、上記の返送汚水量は、エアリフト管(14)と
連結した集水桝(14a)の上下スライド位置調節によ
り調整可能としている。(14h)はスライド用長孔、
(14i)は取付ボルト、(14j)は締付調節用ナツ
トである。
The amount of returned wastewater can be adjusted by adjusting the vertical sliding position of the water collection basin (14a) connected to the air lift pipe (14). (14h) is a long hole for slide,
(14i) is a mounting bolt, and (14j) is a tightening adjustment nut.

また、集水桝(14a)の上面には、第6図に示すよう
に、集水桝1! (14k)を取付けて、同集水桝若(
14k)により集水桝(14a)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(14c)の上方を越えて返送パイプ(14b)
へ直接的に流入するのを防止することができる。
Moreover, as shown in FIG. 6, on the upper surface of the water collection basin (14a), there is a water collection basin 1! (14k) and the same collection Mizumasuwaka (
By closing the upper surface of the water collection basin (14a) with the air lift pipe (14k), the treated water flows from the upper end opening of the air lift pipe (14) over the partition plate (14c) to the return pipe (14b).
can be prevented from directly flowing into the

逆洗管(15)は、好気性沢床(12)の下方に略水平
状に配設した多数の噴出孔を設けた噴出管(15a)の
一端を、好気性処理室(a3)と沈澱分離室(a4)間
の隔壁(3)に沿って垂設した逆洗縦管(15b)の下
端と連7通させ、同逆洗縦管(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ている。
The backwash pipe (15) connects one end of the jet pipe (15a), which has a large number of jet holes arranged substantially horizontally below the aerobic stream bed (12), to the aerobic treatment chamber (a3) and the sedimentation chamber. A flexible pipe (15C ) via the air pipe (13c)
They are supported in a cantilevered manner and communicated with each other.

また、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、同隔壁(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。
In addition, the partition wall (2) between the second chamber (a2) and the aerobic treatment chamber (a3) completely partitions the area below the treated water level (h) of the septic tank body (a), and the second chamber (a2) ) to the aerobic treatment chamber (a3), the advection of the treated water is carried out through the second
This is carried out by a third advection pipe (16) provided on the side surface of the chamber (a2).

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(a2)(
a3)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 and the second
The chamber (a2) and the aerobic treatment chamber (a3) are separated into each chamber (a2) (
It communicates at the top of a3).

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筒(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 the chemical cylinder (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(h)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)に浮上しなスカムが沈澱
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 upper edge protrudes above the treated water surface (h) and the lower edge is immersed below the treated water surface (h) to prevent scum from floating on the treated water surface (h) of the sedimentation separation chamber (a4). 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tn)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 tn) 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(bl)(b2)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(
b3)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
, the second manhole (bl) (b2) is provided so that it can be opened and closed freely,
A small-diameter third manhole (
b3) 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(ロ)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#R物(水、炭水化物、蛋白質、脂質、尿素
を成分とする)は、上向流嫌気性炉床(5)を通過する
間に、同炉床(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cJる。
The treated water flowing into the first chamber (al) from the upstream side of the sewage discharge pipe (b) through the inlet (4) and #R substances (water, carbohydrates, proteins, While passing through the up-flow anaerobic hearth (5), the anaerobic bacteria that adhere to the surface of the furnace material of the hearth (5) undergo anaerobic decomposition. .

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(CH3C00tl )やプロピオン酸(
CHa CH2C0OH)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(C114)や二酸化炭素(CO2)を生成して、
これらの気体を浄化槽(A)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
(NH4” −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 to a low molecular weight by acid-producing bacteria and converted into acetic acid (CH3C00tl) and propionic acid (
CHa CH2C0OH), etc., and then
Anaerobic bacteria such as methane bacteria decompose organic acids to produce methane (C114) and carbon dioxide (CO2).
These gases are discharged to the outside of the septic tank (A), and treated water containing ammonia nitrogen (NH4''-N), which is a decomposition product of protein and the nitrogen component of urea, is generated.

なお、上向流嫌気性炉床(5)゛を通過した処理水中に
含まれる粗大な固形物は第1室(al)の底部に沈澱す
る。
Incidentally, coarse solids contained in the treated water that has passed through the upward flow anaerobic hearth (5) settle 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MN’lJ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(N1
14 ” −N)及び少量の未処理有R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, MN'lJ can be effectively removed from the treated water, and as a result, the treated water after anaerobic treatment contains ammonia nitrogen (N1
14''-N) and a small amount of unprocessed R substances are 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移流管(10)及
び第2移流管(11)を通過して、第2室(a2)の上
向流嫌気性炉床(9)の下方に、同P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 advection pipe (10) and the second advection pipe (11), and flows downward to the upward flow anaerobic hearth (9) in the second chamber (a2). It is directly transferred to the same P bed (9) without any anaerobic treatment.

その後、上向流嫌気性炉床(9)を下がら上へ通過する
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(Ntla
   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(O3)に第3移
流管(16)を介して移送される。
After that, while passing downward and upward through the upward flow anaerobic hearth (9), it undergoes the same anaerobic decomposition as described above again, further decomposing organic matter, and then ammonia (Ntla
The treated water containing N) and a further small amount of untreated organic matter is transferred to the next aerobic treatment chamber (O3) 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
(O2)における嫌気性処理を、処理水を、上自流嫌気
性炉床(9)を下から上へ向けて通過−する上向流とす
ることによって、嫌気性P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鮫して、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 embodiment, the anaerobic treatment in the second chamber (O2) of the anaerobic treatment chamber (C) is performed by passing the treated water through the upper flow anaerobic hearth (9) from bottom to top. By using an upward flow that passes through the anaerobic P bed from the top to the bottom, the flow rate can be lowered, and more undecomposed materials can be transferred to the furnace. It can be moored to the floor to further promote anaerobic decomposition.

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(O2)の底部に直接送
り、第2室(O2)の上部へ送らないで、未分解物が上
向流嫌気性枦床(9)の上部に滞留しなり、第2室(O
2)から、同第2室(O2)に並設した好気性処理室(
O3)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 (O2), without being sent to the top of the second chamber (O2). Undecomposed substances remain in the upper part of the upward flow anaerobic bed (9), and the second chamber (O
2) to the aerobic treatment room (O2) installed in parallel with the second room (O2).
It is possible to reliably prevent the water from flowing directly into O3).

次に、好気性処理室(O3)内における浄化処理につい
て説明すると、好気性処理室(O3)中では、曝気装!
 (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(NH4”−N)は、硝酸態窒(N02−
−N)や亜硝#態窒素(NO2−−N)に酸化分解され
る。
Next, to explain the purification process in the aerobic treatment chamber (O3), inside the aerobic treatment chamber (O3), there is an aeration system!
Air is blown into the treated water from the aeration pipe (13b) in (13), and aerobic bacteria such as nitrifying bacteria utilize the oxygen in the air to oxidize and decompose the ammonia nitrogen ( NH4''-N) is nitrate nitrogen (N02-
-N) and nitrite (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P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。
It is also preferable to inoculate aerobic bacteria with a proven seed bacteria as described above, and the aerobic P bed (12) will allow the aerobic bacteria to adhere to it, causing the aerobic bacteria to flow out, thereby reducing the bacterial concentration. 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(^)外に
放流することなく、好気性処理室(O3)中で好気分解
処理中の処理水の一部(O2)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ンの上方に配設した集水桝
(14a)に持ち上げ、同集水桝(14a)で気液分離
し、その後、返送パイプ(14C)を介して第1室(a
l)に返送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 (O3) without being directly discharged outside the septic tank (^). A part of the treated water (O2) is transferred to the air lift pipe (14
The air from the diffuser pipe (13b) that is blown into the air lift pipe (14) from below lifts the air to the water collection basin (14a) installed above the air lift pipe (14), where the air and liquid are separated in the water collection basin (14a). , the first chamber (a) via the return pipe (14C)
I am trying to send it back to l).

しかして、硝酸態窒素(803’″−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、!!機機台合物還元されて分子状窒素(
N2)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 (803'''-N) and nitrite nitrogen <NO2--N) flows into the first chamber (al), the amount of water present in the first chamber (al) Denitrifying bacteria utilizes the oxygen of these inorganic compounds to decompose the organic matter that flows into the first chamber (al) to obtain energy for survival.As a result, the denitrifying bacteria is reduced to organic matter and molecules Nitrogen (
N2) and nitrous oxide (N20), organic carbon is decomposed and becomes carbon dioxide (CO2), and the septic tank (A)
It will be released outside.

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(O3)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。
In this way, the decomposition treatment of organic matter in the first chamber (al) can be performed not only by anaerobic treatment but also by partially refluxed water from the aerobic treatment chamber (O3) and denitrifying bacteria acting on it.

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(NH4” −N)の過剰増加
(これは嫌気性菌の活性を抑制する方向に面<)を抑え
ることができ、また、かが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。
Therefore, it is possible to suppress the excessive increase in ammonia nitrogen (NH4''-N) that occurs when performing anaerobic treatment using only anaerobic bacteria (this is in the direction of suppressing the activity of anaerobic bacteria), Further, due to the 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(O3)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(
O3)内の汚泥の発生も可及的に低減することができる
In addition, by improving the ability to decompose organic matter, the amount of untreated organic matter contained in the treated water transferred from the anaerobic treatment chamber (C) to the aerobic treatment chamber (O3) can be significantly reduced. Aerobic treatment room due to untreated organic matter (
The generation of sludge in O3) can also be reduced as much as possible.

一方、好気性処理室(O3)における処理水中の硝酸態
窒素(NO3−−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(N20)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, the concentration of nitrate nitrogen (NO3--N) and nitrite nitrogen (NO2-N) in the treated water in the aerobic treatment room (O3) also decreased when some of the treated water was transferred to the anaerobic treatment room (C). Reflux and convert those ions into molecular nitrogen (N2) by denitrifying bacteria.
Since it can be decomposed into nitrous oxide (N20) and nitrous oxide (N20), 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(a4)の下部に流入し
、処理水中に残留した極めてIR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(
18b)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 (a4), rises while precipitating a very large amount of solid matter remaining in the treated water, flows into the disinfection chamber (18), and enters the chemical cylinder. (
18b) 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(a4)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(a4
)の内底面を好気性処理室(a3)の方向へ下り急傾斜
させたことで、同沈澱分離室(a4)中の沈澱汚泥は好
気性処理室(a3)の底部ケ移動させるようにしている
In addition, by making the sedimentation separation chamber (a4) a riser type, sludge brackets are generated and can be collected even with relatively light specific gravity and small flocs.
) is steeply sloped downward in the direction of the aerobic treatment chamber (a3), so that the settled sludge in the sedimentation separation chamber (a4) is moved to the bottom of the aerobic treatment chamber (a3). 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(a3)中の処理
水の一部を還流する構成とじているので、BOD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 (a3). Since a part of the treated water is refluxed, the BOD 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
(A)によって得られた最終処理水中におけるBODf
4度等は、以下の表に示す通りであつた。
According to experiments conducted by the applicant, BODf in the final treated water obtained by the septic tank (A) according to this example
4 degrees etc. 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.

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B(>T)濃度等を著しく低減する
ことができる。
As is clear from the above table, in the case of this example, the B (>T) 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(a3)から嫌気性処理室(C)へ
の一部還流量を(02)とすれば、嫌気性処理室(C)
から好気性処理室(a3)に移送される処理水の景(Q
3)は、Q3= 01+ 02となるが、Ql : Q
2=〜1:1〜10(最適には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 (a3) to the anaerobic treatment chamber (C) is (02), then the anaerobic treatment chamber (C)
A view of the treated water being transferred from the to the aerobic treatment room (a3) (Q
3) becomes Q3=01+02, but Ql : Q
It has been found that it is preferable that 2=~1:1-10 (optimally 1:2-6).

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(a2)、好気性
処理室(a3)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 remains of exfoliated bacteria accumulates in the first chamber (al), the second chamber (a2), and the aerobic treatment chamber (a3).

、二の場合は、蓋体(b)の第1、第2マンホール(b
IHb2)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(a2)
の底部に固形物や汚泥を吸い収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(
a3)中の固形物や汚泥を吸い取ることで、沈澱分離室
(a4)の固形物も同時に吸い取られる。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 the case of 2, the first and second manholes (b) of the lid body (b)
Open IHb2) and connect the first and second advection tubes (10) (11)
By making the passageway, the first chamber (al) and the second chamber (a2)
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 a3), the solids in the sedimentation separation chamber (a4) are also sucked out 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、
可撓性パイプ(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 pipe (15c), the excess sludge can be reliably washed away.

(へ)効果 本発明では、流入口の直下方に、流入口からの流入汚水
を受止める状態で邪魔板を配設し、同邪魔板で一旦汚水
を受止めて浄化処理部へ流下させるようにしているなめ
に、以下のような作用効果が生起される。
(f) Effect In the present invention, a baffle plate is disposed directly below the inlet to catch the wastewater flowing in from the inlet, and the baffle plate temporarily catches the wastewater and allows it to flow down to the purification processing section. Because of this, the following effects occur.

■汚水が浄化処理部中を直線的に通過するのを防止する
ことができ、同浄化処理部による汚水の嫌気性処理を確
実に行なわせることができる。特に、流入汚水中の固形
物を邪魔板により分散させて、嫌気性処理能力を良好に
確保することができる。
(2) It is possible to prevent sewage from passing linearly through the purification treatment section, and the anaerobic treatment of the sewage can be reliably performed by the purification treatment section. In particular, by dispersing the solids in the inflowing wastewater using the baffle plates, good anaerobic treatment capacity can be ensured.

■汚水が直線的に流入することによる浄化槽本体内の汚
水中への空気の巻込みを防止することができるために、
同汚水中の溶存酸素量が増大して嫌気性菌の活性が抑制
されるという不具合の発生を防止することができる。
■It is possible to prevent air from being drawn into the sewage inside the septic tank due to the linear inflow of sewage.
It is possible to prevent the occurrence of a problem in which the amount of dissolved oxygen in the wastewater increases and the activity of anaerobic bacteria is suppressed.

■浄化槽本体内の汚水面に形成されたスカム層が、直線
的に流入する汚水によって破壊されるという不具合の発
生を防止することができ、同スカム層による浄化槽本体
内の汚水と空気との接触防止を良好に確保して、浄化槽
本体内における嫌気性処理能力を良好に確保することが
できる。
■It is possible to prevent the occurrence of problems in which the scum layer formed on the sewage surface inside the septic tank body is destroyed by the sewage flowing in linearly, and the scum layer causes contact between the sewage inside the septic tank body and the air. Prevention can be ensured well, and anaerobic treatment capacity within the septic tank body can be ensured well.

■汚水落下時に、同汚水が浄化槽本体内に溜っている汚
水に直接衝突することがなくなるために、騒音の発生を
防止することができる。
■When sewage falls, it no longer directly collides with the sewage collected inside the septic tank body, so it is possible to prevent the generation of noise.

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

第1図は、本発明による邪魔板構造を具伽する浄化槽の
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、邪魔板の拡大斜視図。 第5図は、好気性処理室の平面図。 第6図は、集水桝の斜視図。 第7図は、 他の実施例と しての集水桝の斜視図。 (^):浄化槽 (C):嫌気性処理室 (at):第1室 (a2):第2室 a3):好気性処理室 a4):沈澱分離室 1):隔壁 10):第1移流管 11):第2移流管 18):消毒室 25)二邪魔板
FIG. 1 is a cross-sectional side view of a septic tank equipped with a baffle plate 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 an enlarged perspective view of the baffle plate. FIG. 5 is a plan view of the aerobic treatment chamber. Figure 6 is a perspective view of the water collection basin. FIG. 7 is a perspective view of a water collection basin as another embodiment. (^): Septic tank (C): Anaerobic treatment chamber (at): First chamber (a2): Second chamber a3): Aerobic treatment chamber a4): Sedimentation separation chamber 1): Partition wall 10): First advection Pipe 11): Second advection pipe 18): Disinfection chamber 25) Two baffles

Claims (1)

【特許請求の範囲】 1)浄化槽本体(a)の一側に、汚水排出管路の上流側
と連通する流入口(4)を設けると共に、同浄化槽本体
(a)の他側に、汚水排出管路の下流側と連通する放流
口(17)を設け、上記流入口(4)より浄化槽本体(
a)内に流入する汚水を、同浄化槽本体(a)に設けた
浄化処理部により浄化処理して放流口(17)より汚水
排出管路の下流側へ放流すべく構成した浄化槽において
、 流入口(4)の直下方に、流入口(4)からの流入汚水
を受止める状態で邪魔板(25)を配設し、同邪魔板(
25)で一旦汚水を受止めて浄化処理部へ流下させるべ
く構成してなる浄化槽における邪魔板構造。 2)請求項1記載の邪魔板(25)を、放流口(17)
側に向けて前低後高に傾斜させたことを特徴とする浄化
槽における邪魔板構造。
[Claims] 1) An inlet (4) communicating with the upstream side of the sewage discharge pipe is provided on one side of the septic tank body (a), and a sewage discharge port is provided on the other side of the septic tank body (a). A discharge port (17) communicating with the downstream side of the pipeline is provided, and the septic tank body (
a) In a septic tank configured to purify the sewage flowing into the septic tank by a septic processing section provided in the septic tank body (a) and discharge it from the outlet (17) to the downstream side of the sewage discharge pipe, the inlet A baffle plate (25) is arranged directly below the inlet (4) to catch the inflowing wastewater from the inlet (4).
25) A baffle plate structure in a septic tank configured to once receive sewage and flow it down to a purification treatment section. 2) The baffle plate (25) according to claim 1 is connected to the outlet (17).
A baffle plate structure in a septic tank characterized by being inclined toward the side with a low front and a high rear.
JP4395189A 1989-02-25 1989-02-25 Baffle plate structure for septic tank Pending JPH02222778A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4395189A JPH02222778A (en) 1989-02-25 1989-02-25 Baffle plate structure for septic tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4395189A JPH02222778A (en) 1989-02-25 1989-02-25 Baffle plate structure for septic tank

Publications (1)

Publication Number Publication Date
JPH02222778A true JPH02222778A (en) 1990-09-05

Family

ID=12678014

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4395189A Pending JPH02222778A (en) 1989-02-25 1989-02-25 Baffle plate structure for septic tank

Country Status (1)

Country Link
JP (1) JPH02222778A (en)

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