JPH0222072Y2 - - Google Patents
Info
- Publication number
- JPH0222072Y2 JPH0222072Y2 JP1986126054U JP12605486U JPH0222072Y2 JP H0222072 Y2 JPH0222072 Y2 JP H0222072Y2 JP 1986126054 U JP1986126054 U JP 1986126054U JP 12605486 U JP12605486 U JP 12605486U JP H0222072 Y2 JPH0222072 Y2 JP H0222072Y2
- Authority
- JP
- Japan
- Prior art keywords
- chamber
- weir
- water
- sewage treatment
- publication
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 38
- 238000004062 sedimentation Methods 0.000 claims description 12
- 239000010865 sewage Substances 0.000 claims description 11
- 238000000926 separation method Methods 0.000 claims description 9
- 238000004659 sterilization and disinfection Methods 0.000 claims description 4
- 238000000034 method Methods 0.000 description 11
- 239000010802 sludge Substances 0.000 description 5
- 238000005273 aeration Methods 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 2
- 238000007654 immersion Methods 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 230000001133 acceleration Effects 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000004299 exfoliation Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000010800 human waste Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Treatment Of Biological Wastes In General (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
- Biological Treatment Of Waste Water (AREA)
Description
【考案の詳細な説明】
〔産業上の利用分野〕
本考案は、好気処理室において剥離した生物膜
を含む混合液を沈澱分離室または嫌気処理室に返
送する汚水処理装置の改良に係るものである。[Detailed description of the invention] [Industrial application field] The present invention relates to an improvement of a sewage treatment device that returns a mixed liquid containing biofilm detached in an aerobic treatment chamber to a sedimentation separation chamber or an anaerobic treatment chamber. It is.
従来、汚水の生物学的処理といえば、活性汚泥
法が最も一般的であつたが、近年ある種の支持体
(床)に活性汚泥を固定して生物膜を形成させ、
これに汚水を接触させて浄化する生物膜方式が普
及しつつある。なかでも床を水中に浸漬させた
接触ばつ気方式は維持管理が容易であるほか、負
荷や温度の急激な変化にも対応力のある優れた方
式である。反面生物膜の過剰着床による床の閉
塞や、剥離による処理水質の悪化等は避けられな
いため、剥離した汚泥を含む好気処理水を常時ま
たは間欠的に前処理である沈澱分離室又は嫌気処
理室に返送し、剥離汚泥を沈澱分離除去しようと
する方法が採用されている。
Traditionally, activated sludge method was the most common biological treatment of sewage, but in recent years activated sludge has been fixed on a certain kind of support (bed) to form a biofilm.
The biofilm method, which purifies wastewater by bringing it into contact with wastewater, is becoming popular. Among these, the contact aeration method, in which the floor is immersed in water, is easy to maintain and is an excellent method that can withstand rapid changes in load and temperature. On the other hand, blockage of the floor due to excessive biofilm deposition and deterioration of treated water quality due to exfoliation are unavoidable, so aerobic treated water containing exfoliated sludge is constantly or intermittently treated in a sedimentation separation chamber or anaerobic. A method is adopted in which the separated sludge is sent back to the treatment room and separated and removed by sedimentation.
好気処理水を沈澱分離室に返送する方法として
は、「屎尿浄化槽の構造基準・同解設(1980年
版)」(日本建築センター)第134頁に記載の液
面のリストアツプによる自然返送、エアリフト
ポンプによる強制返送がある。 Methods for returning aerobic treated water to the sedimentation separation room include natural return by restoring the liquid level as described in "Structural Standards and Disassembly of Human Waste Septic Tanks (1980 Edition)" (Japan Building Center), page 134; There is a forced return using an air lift pump.
また、公報としては下記のものが有る。 Additionally, there are the following publications:
1 液面のリフトアツプを利用したもの
1 実公昭61−10800号公報
2 実開昭60−21394号公報
3 実公昭60−39118号公報
4 実公昭60−4760号公報
5 特開昭59−93789号公報
6 実開昭59−93789号公報
7 実開昭58−86298号公報
8 実開昭58−31096号公報
9 実開昭57−199098号公報
10 実開昭57−177598号公報
2 水流を利用したもの
1 特公昭58−6555号公報
2 実公昭57−14952号公報
3 水面の上下によるもの
1 実公昭58−17674号公報
4 強制エアリフトによるもの
1 実開昭59−44592号公報
2 実開昭58−156591号公報
5 自然エアリフトによるもの(本考案と最も近
い技術)
1 実公昭58−26074号公報
2 実公昭60−10714号公報
〔考案が解決しようとする問題点〕
一方、前記の発明又は考案、即ち1に示す液面
のリフトアツプを利用した方式(第5図)、およ
び2に示す水流を利用した方式(第3図)は、設
置時の槽の傾きや、散気装置のずれ、接触材の閉
塞等による水流の偏りにより定量的な返送が出来
ないという問題点があつた。また3に示す水面の
上下による方法も同様の問題点を有している。一
方エアリフトを使つたもの(第4図,第6図)
は、定量性はあるものの少ない吐出量例えば1
/分程度においては空気量の調整が難かしく、
長期間の安定した吐出量を得ることができないと
いう問題点があつた。例えば実公昭58−26074号
公報はエアリフト方式の自然返送(第6図)であ
るが、返送量の制御は困難である。また実公昭60
−10714号公報も前号とほぼ同じ方式のエアリフ
ト自然返送であるが、アタツチメントの着脱によ
つて返送の有無を行うため少量の常時返送を行う
ことには無理がある。1 Utilizing lift-up of the liquid level 1 Publication of Utility Model Publication No. 1988-10800 2 Publication of Publication of Japanese Utility Model No. 60-21394 3 Publication of Publication of Publication of Japanese Utility Model No. 39118-1984 4 Publication of Publication of Publication of Japanese Utility Model No. 60-4760 5 Publication of Japanese Utility Model Publication No. 59-93789 Publications 6 Utility Model Application Publication No. 59-93789 7 Utility Model Application Publication No. 58-86298 8 Utility Model Application Publication No. 58-31096 9 Utility Model Application Publication No. 57-199098 10 Utility Model Application Publication No. 57-177598 2 Utilizing water flow 1 Japanese Utility Model Publication No. 58-6555 2 Publication of Utility Model Publication No. 57-14952 3 Due to the rise and fall of the water surface 1 Publication of Utility Model Publication No. 58-17674 4 Due to forced air lift 1 Publication of Utility Model Publication No. 59-44592 2 Utility Model Publication Publication No. 58-156591 5 Based on natural air lift (technology closest to the present invention) 1 Publication of Utility Model Publication No. 58-26074 2 Publication of Publication of Utility Model No. 60-10714 [Problems to be solved by the invention] On the other hand, the above-mentioned invention or The two methods, namely, the method using liquid level lift-up shown in 1 (Fig. 5) and the method using water flow shown in 2 (Fig. 3), are designed to prevent the inclination of the tank during installation, the misalignment of the air diffuser, There was a problem in that quantitative return was not possible due to uneven water flow due to blockage of the contact material, etc. Further, the method shown in 3, which involves raising and lowering the water surface, has similar problems. On the other hand, those using air lift (Fig. 4, Fig. 6)
is a quantitative but small discharge amount, for example 1
/ minute, it is difficult to adjust the air volume.
There was a problem that a stable discharge amount could not be obtained for a long period of time. For example, Japanese Utility Model Publication No. 58-26074 uses an air lift system for natural return (FIG. 6), but it is difficult to control the amount of return. Also, Jiko 60
Publication No. 10714 also uses airlift natural return, which is almost the same method as the previous issue, but it is impossible to constantly return small quantities because the return is determined by attaching and detaching the attachment.
本考案は上記欠点に鑑みてなされたものであ
り、他の動力なしで好気処理水を沈澱分離室また
は嫌気処理室に少量の返送ができ、しかも返送量
のばらつきのない汚水処理装置を安価に提供する
ことを目的としたものである。 The present invention was developed in view of the above-mentioned drawbacks, and provides a sewage treatment system that can return a small amount of aerobically treated water to a sedimentation separation chamber or an anaerobic treatment chamber without any other power, and that does not vary in the amount of returned water at a low cost. It is intended to provide.
上記の目的を達成するための本考案の構成を、
実施例に対応する第1図及び第2図に基き説明す
ると、本考案は、沈澱分離室及び/又は嫌気処理
室1、好気処理室2、沈澱室3、消毒室4をこの
順に配置してなる汚水処理装置20において、好
気処理室2内に配置された散気装置5の直上部に
下端開口部を臨ませたライザー管6の上部に上下
方向調整可能な流量調整用容器7を取付け、該容
器7には余剰水戻し用の幅広堰9、整流用バツフ
ル10及び返送水計量堰11とを設けた技術手段
を講じている。
The structure of the present invention to achieve the above purpose is as follows:
To explain based on FIG. 1 and FIG. 2 corresponding to the embodiment, the present invention has a sedimentation separation chamber and/or an anaerobic treatment chamber 1, an aerobic treatment chamber 2, a precipitation chamber 3, and a disinfection chamber 4 arranged in this order. In the sewage treatment equipment 20, a flow rate adjustment container 7 that can be adjusted in the vertical direction is installed at the top of the riser pipe 6 whose lower end opening faces directly above the aeration device 5 disposed in the aerobic treatment chamber 2. Attachment, technical measures are taken in which the container 7 is provided with a wide weir 9 for returning excess water, a rectification baffle 10, and a return water measuring weir 11.
以下、本考案の実施例を第1図、第2図に従つ
て詳述する。第1図は本考案の一実施例を示す流
量調整用容器の斜視図、第2図は流量調整用容器
の取付状態を示す断面図である。
Hereinafter, embodiments of the present invention will be described in detail with reference to FIGS. 1 and 2. FIG. 1 is a perspective view of a flow rate adjustment container showing an embodiment of the present invention, and FIG. 2 is a sectional view showing the installed state of the flow rate adjustment container.
20は、沈澱分離室及び/又は嫌気処理室1、
内部に床17及び散気装置5を設けた好気処理
室2、沈澱室3、消毒室4よりなる汚水処理装置
である。 20 is a precipitation separation chamber and/or an anaerobic treatment chamber 1;
This sewage treatment equipment consists of an aerobic treatment chamber 2, a sedimentation chamber 3, and a disinfection chamber 4, each of which is equipped with a floor 17 and an air diffuser 5.
好気処理室2に酸素を供給するための散気装置
5近傍のほぼ直上部に下端が開口されたライザー
管6が設けられている。散気装置5から吐出する
空気は、そのほとんどは好気処理室2への酸素の
供給及び水流を発生させるためのエネルギー源と
して使用されるが、一部はライザー管6の開口下
端より管内部に進入し、管内外の液比重差によ
り、ライザー管6にエアリフト現象が生ずる。こ
の結果、好気処理水はライザー管6と一体の流量
調整用容器7に揚水される。流量調整用容器7の
内部には、整流用バツフル10を挾んで余剰水戻
し用の幅広堰9と返送量をチエツクするための計
量堰11が設けてある。これらの堰の長さの差に
より、流量調整用容器7内の水位は、幅広堰9に
より決定され、ライザー管6内の揚水量が変化し
た場合でも、ほぼ定水位を保つようになる。この
結果返送水計量堰11における水頭は一定とな
り、定量的に好気処理水を沈澱分離室または嫌気
処理室1(図では省略)に返送できるようにな
る。このためには計量堰11は三角堰であること
が望ましい。 A riser pipe 6 whose lower end is open is provided almost directly above the air diffuser 5 for supplying oxygen to the aerobic treatment chamber 2 . Most of the air discharged from the aeration device 5 is used as an energy source for supplying oxygen to the aerobic treatment chamber 2 and generating water flow, but some of it is used as an energy source for supplying oxygen to the aerobic treatment chamber 2 and for generating water flow, but some of the air is used for supplying oxygen to the aerobic treatment chamber 2 and as an energy source for generating water flow. The air lift phenomenon occurs in the riser pipe 6 due to the difference in specific gravity between the inside and outside of the pipe. As a result, the aerobically treated water is pumped into the flow rate adjustment container 7 integrated with the riser pipe 6. Inside the flow rate adjustment container 7, a wide weir 9 for returning excess water and a measuring weir 11 for checking the amount of returned water are provided, sandwiching the rectification baffle 10. Due to the difference in the lengths of these weirs, the water level in the flow rate regulating container 7 is determined by the wide weir 9, and even when the amount of water pumped in the riser pipe 6 changes, it maintains a substantially constant water level. As a result, the water head at the return water metering weir 11 becomes constant, making it possible to quantitatively return aerobic treated water to the sedimentation separation chamber or anaerobic treatment chamber 1 (not shown). For this purpose, it is desirable that the weighing weir 11 be a triangular weir.
一般にエアリフトポンプの揚水量は浸水深さ
Hsと揚程Hで示されるHs/Hs+H(浸水率)に大
きく影響されることが判つている。又、通常の状
態では揚程Hは大きくする必要はないから、本考
案のようにライザー管6を散気装置5の真上部に
まで浸漬させることは浸水率を一定に保つのに効
果的である。また、流量調整用容器7は調整ねじ
8により容易に上下できるから、散気装置5の目
詰り等に対しても容易に対応できる。 In general, the amount of water pumped by an air lift pump depends on the immersion depth.
It is known that it is greatly influenced by Hs/Hs+H (submergence rate), which is expressed by Hs and head H. Also, under normal conditions, there is no need to increase the head H, so immersing the riser pipe 6 to the top of the diffuser 5 as in the present invention is effective in keeping the water immersion rate constant. . Further, since the flow rate adjusting container 7 can be easily moved up and down using the adjusting screw 8, it is possible to easily deal with clogging of the air diffuser 5, etc.
第7図及び第8図は、本考案の他の実施例を示
す斜視図である。第7図では、前述の第1図に示
す幅広堰9をバツフル10の両側に設けてあるた
め、ライザー管6内の揚水量が過大であつても余
剰水はすみやかに幅広堰9より好気処理室2に戻
され安定した返送水量を得ることが出来る。第8
図はバツフル10の代りにオリフイス18を設け
たものである。一般にオリフイスより流出する水
量θは、オリフイスの断面積Aと水位Hとの間に
Q=A・C√2g(g:重力加速度、C:流量
係数)の関係があるので断面積A又は堰の高さを
変えることにより返送水量の調整が可能で、また
第7図と同様にライザー管6内の過大な揚水量に
おいても安定した返送水量が得られる。 7 and 8 are perspective views showing other embodiments of the present invention. In FIG. 7, the wide weir 9 shown in FIG. It is possible to obtain a stable amount of water returned to the treatment chamber 2. 8th
In the figure, an orifice 18 is provided in place of the buttful 10. In general, the amount of water θ flowing out from an orifice is determined by the relationship between the cross-sectional area A of the orifice and the water level H as Q=A・C√2g (g: gravitational acceleration, C: flow rate coefficient). By changing the height, the amount of returned water can be adjusted, and as in FIG. 7, a stable amount of returned water can be obtained even when the amount of water pumped in the riser pipe 6 is excessive.
本考案は、好気処理室内に配設された散気装置
の直上部に下端開口部を臨せたライザー管の上部
に流量調整用容器を取付け、該容器には余剰水戻
し用の堰、整流用バツフル及び返送水計量堰とを
設けた構成としたので、新規な動力なしで好気処
理水を沈澱分離室又は嫌気処理室に少量(1/
分程度)の返送が可能になるとともに返送量のば
らつき(変動係数=標準偏差/平均値×100が3%以下
)
が極めて小さい汚水処理装置を安価に提供できる
効果を奏するものである。
In the present invention, a flow rate adjustment container is attached to the top of a riser pipe whose lower end opening is directly above an aeration device installed in an aerobic treatment room, and a weir for returning excess water is installed in the container. Since the configuration is equipped with a rectifying butthole and a return water metering weir, a small amount (1/2
This has the effect of making it possible to provide a wastewater treatment equipment at a low cost, which allows for a return of approximately 30 minutes (about 30 minutes), and has an extremely small variation in return amount (coefficient of variation = standard deviation/average value x 100 of 3% or less).
第1図は本考案の実施例を示す斜視図、第2図
は本考案の実施例を示す略断面図、第3図乃至第
6図は従来の実施例を示す略断面図、第7図、第
8図は本考案の他の実施例を示す斜視図である。
符号の説明、1……沈澱分離室、2……好気処
理室、3……沈澱室、4……消毒室、5……散気
装置、6……ライザー管、7……流量調整用容
器、8……調整ねじ、9……幅広堰、10……バ
ツフル、11……計量堰、12……汚泥、13…
…移流管、14……エアリフトバツフル、15…
…エアリフトパイプ、16……調整バツフル、1
7……床、18……オリフイス、20……汚水
処理装置。
FIG. 1 is a perspective view showing an embodiment of the present invention, FIG. 2 is a schematic sectional view showing an embodiment of the present invention, FIGS. 3 to 6 are schematic sectional views showing a conventional embodiment, and FIG. , FIG. 8 is a perspective view showing another embodiment of the present invention. Explanation of symbols, 1...Sedimentation separation chamber, 2...Aerobic treatment room, 3...Sedimentation chamber, 4...Disinfection room, 5...Air diffuser, 6...Riser pipe, 7...For flow rate adjustment Container, 8...Adjusting screw, 9...Wide weir, 10...Bassful, 11...Measuring weir, 12...Sludge, 13...
...Advection tube, 14...Airlift Batsuful, 15...
...air lift pipe, 16...adjustment full, 1
7...floor, 18...orifice, 20...sewage treatment equipment.
Claims (1)
室、沈澱室、消毒室をこの順に配置してなる汚
水処理装置において、好気処理室内に配設され
た散気装置の直上部に下端開口部を臨せたライ
ザー管の上部に流量調整用容器を取付け、該容
器には余剰水戻し用の堰、整流用バツフル及び
返送水計量堰とを設けたことを特徴とする汚水
処理装置。 2 流量調整用容器が、上下方向調整可能にライ
ザー管に取付けられたものであることを特徴と
する実用新案登録請求の範囲第1項記載の汚水
処理装置。 3 余剰水戻し用堰が、幅広堰であることを特徴
とする実用新案登録請求の範囲第1項記載の汚
水処理装置。 4 ライザー管の下端開口部が、散気装置の近傍
に位置させたことを特徴とする実用新案登録請
求の範囲第1項記載の汚水処理装置。[Scope of Claim for Utility Model Registration] 1. In a sewage treatment system consisting of a sedimentation separation chamber and/or an anaerobic treatment chamber, an aerobic treatment chamber, a sedimentation chamber, and a disinfection chamber arranged in this order, A flow rate adjustment container is attached to the top of the riser pipe whose lower end opening is directly above the air diffuser, and the container is equipped with a weir for returning excess water, a rectifying buttful, and a return water measuring weir. A sewage treatment device featuring: 2. The sewage treatment device according to claim 1, wherein the flow rate adjusting container is attached to the riser pipe so as to be adjustable in the vertical direction. 3. The sewage treatment device according to claim 1, wherein the surplus water return weir is a wide weir. 4. The sewage treatment device according to claim 1, wherein the lower end opening of the riser pipe is located near the air diffuser.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1986126054U JPH0222072Y2 (en) | 1986-08-19 | 1986-08-19 |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1986126054U JPH0222072Y2 (en) | 1986-08-19 | 1986-08-19 |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6332699U JPS6332699U (en) | 1988-03-02 |
JPH0222072Y2 true JPH0222072Y2 (en) | 1990-06-13 |
Family
ID=31019503
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1986126054U Expired JPH0222072Y2 (en) | 1986-08-19 | 1986-08-19 |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0222072Y2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001329999A (en) * | 2000-05-23 | 2001-11-30 | Hitachi Chem Co Ltd | Fluid transfer device |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0626396Y2 (en) * | 1988-04-23 | 1994-07-20 | 進 坪内 | Sewage treatment equipment |
JPH061280Y2 (en) * | 1989-05-09 | 1994-01-12 | 進 坪内 | Household miscellaneous wastewater treatment equipment |
-
1986
- 1986-08-19 JP JP1986126054U patent/JPH0222072Y2/ja not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001329999A (en) * | 2000-05-23 | 2001-11-30 | Hitachi Chem Co Ltd | Fluid transfer device |
Also Published As
Publication number | Publication date |
---|---|
JPS6332699U (en) | 1988-03-02 |
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