JPH0673678B2 - Biological treatment tank - Google Patents

Biological treatment tank

Info

Publication number
JPH0673678B2
JPH0673678B2 JP2411972A JP41197290A JPH0673678B2 JP H0673678 B2 JPH0673678 B2 JP H0673678B2 JP 2411972 A JP2411972 A JP 2411972A JP 41197290 A JP41197290 A JP 41197290A JP H0673678 B2 JPH0673678 B2 JP H0673678B2
Authority
JP
Japan
Prior art keywords
wastewater
biological treatment
sludge
section
partition wall
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP2411972A
Other languages
Japanese (ja)
Other versions
JPH04222695A (en
Inventor
進 梶田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
NGK Insulators Ltd
Original Assignee
NGK Insulators 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 NGK Insulators Ltd filed Critical NGK Insulators Ltd
Priority to JP2411972A priority Critical patent/JPH0673678B2/en
Publication of JPH04222695A publication Critical patent/JPH04222695A/en
Publication of JPH0673678B2 publication Critical patent/JPH0673678B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Description

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

【0001】[0001]

【産業上の利用分野】本発明は、下水等の有機性廃水の
処理に用いられる生物処理槽に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a biological treatment tank used for treating organic wastewater such as sewage.

【0002】[0002]

【従来の技術】下水中の汚濁成分を分離除去して下水を
清澄で安全なものに変える方法として、いわゆる活性汚
泥法が知られている。これは曝気槽(エアレーションタ
ンク)中へと流入した下水に、微生物を主体として構成
された活性汚泥を混合し、底部より圧縮空気を気泡とし
て注入するものである。こうして下水と活性汚泥とを混
合攪拌すると共に、空気中の酸素により活性汚泥中の好
気性微生物の活性度を高め、その作用によって浮遊性、
溶解性微生物を凝集、吸着、酸化させる。
2. Description of the Related Art A so-called activated sludge method is known as a method for separating and removing pollutant components in sewage and converting the sewage into a clear and safe one. This is to mix sewage flowing into an aeration tank (aeration tank) with activated sludge composed mainly of microorganisms, and inject compressed air as bubbles from the bottom. In this way, the sewage and the activated sludge are mixed and stirred, and the activity of aerobic microorganisms in the activated sludge is increased by oxygen in the air.
Aggregates, adsorbs and oxidizes soluble microorganisms.

【0003】こうした用途に用いられる曝気槽として、
例えば第3図に概略的に示す曝気槽が知られている。即
ち、タンク21内には例えば略円筒状の隔壁22が設けら
れ、この隔壁22によって、タンク21内は大体、生物処理
部10、汚泥沈澱部13及び処理水上昇路15に区分される。
そして、下水等の廃水を矢印Aのように生物処理部10内
へと導入し、この廃水を活性汚泥と混合すると共に、生
物処理部10の底部に設置した散気装置8から空気を供給
する。生物処理後の廃水は汚泥沈澱部13へと送り込ま
れ、ここで廃水中の汚泥が沈積し、汚泥から分離された
処理水が矢印Gのように処理水上昇路15を上昇する。
この後、水位7まで達した処理水は、処理水受け部21a
へと流入し、矢印Hのように装置外へと排出される。タ
ンク21の底部からは、矢印Fのように随時汚泥を抜く。
なお、図中、6は汚泥掻寄機である。
As an aeration tank used for such purposes,
For example, an aeration tank schematically shown in FIG. 3 is known. That is, for example, a substantially cylindrical partition wall 22 is provided in the tank 21, and the partition wall 22 divides the tank 21 into a biological treatment section 10, a sludge settling section 13, and a treated water rising path 15.
Then, wastewater such as sewage is introduced into the biological treatment unit 10 as indicated by arrow A, the wastewater is mixed with activated sludge, and air is supplied from the air diffuser 8 installed at the bottom of the biological treatment unit 10. . The wastewater after the biological treatment is sent to the sludge settling section 13, where the sludge in the wastewater is deposited, and the treated water separated from the sludge rises up the treated water ascending path 15 as indicated by arrow G.
After this, the treated water that has reached the water level 7 is treated water receiving portion 21a.
And is discharged to the outside of the device as indicated by an arrow H. From the bottom of the tank 21, the sludge is removed at any time as indicated by arrow F.
In the figure, 6 is a sludge scraper.

【0004】[0004]

【発明が解決しようとする課題】しかし、図2に示すよ
うな装置では、汚泥沈澱部13内の汚泥を生物処理部10へ
と巻き上げることがあり、汚泥沈澱の効率が低下する。
また、活性汚泥を生物処理部10へと返送する必要があ
る。
However, in the apparatus as shown in FIG. 2, the sludge in the sludge settling section 13 may be wound up to the biological treatment section 10, which lowers the sludge settling efficiency.
Further, it is necessary to return the activated sludge to the biological treatment section 10.

【0005】本発明の課題は、汚泥沈澱部中に沈積した
汚泥の巻き上げを防止して汚泥沈澱効率を向上させるこ
とができ、また活性汚泥の生物処理槽への返送を不必要
又はごく僅かとできるような廃水処理装置を提供するこ
とである。
The object of the present invention is to prevent the sludge accumulated in the sludge settling section from being rolled up to improve the sludge settling efficiency, and also to make the activated sludge return to the biological treatment tank unnecessary or insignificant. It is to provide such a wastewater treatment device.

【0006】[0006]

【課題を解決するための手段】本発明は、好気性微生物
を含有する活性汚泥と、生物処理部内へ流入する廃水と
を混合し、この廃水内の有機物を生物処理する生物処理
部;前記廃水へと空気を吹き込むために、前記生物処理
部内に配置された散気装置;前記生物処理部に対して第
一の隔壁によって区分された廃水上昇路であって、前記
生物処理後の廃水を上昇させるための廃水上昇路;この
廃水上昇路に対して第二の隔壁によって区分された廃水
下降路であって、この廃水上昇路の上端へと上昇した廃
水を下降させるための廃水下降路;前記生物処理部の下
方に形成された汚泥沈澱部であって、前記生物処理部に
対して第三の隔壁によって隔離され、前記廃水下降路の
下端と連通する汚泥沈澱部;及びこの汚泥沈澱部を通過
した後の処理水を上昇させるための処理水上昇路であっ
て、前記生物処理部に対して第四の隔壁によって隔離さ
れた処理水上昇路を有する、生物処理槽に係るものであ
る。
The present invention relates to a biological treatment section for mixing activated sludge containing aerobic microorganisms with wastewater flowing into the biological treatment section to biologically treat organic matter in the wastewater; An air diffuser disposed in the biological treatment section for blowing air into the biological treatment section; a wastewater ascending path divided by the first partition wall with respect to the biological treatment section to raise the wastewater after the biological treatment. A wastewater ascending path for causing the wastewater ascending path; a wastewater descending path divided by the second partition wall with respect to the wastewater ascending path, and a wastewater descending path for descending the wastewater rising to the upper end of the wastewater ascending path; A sludge sedimentation part formed below the biological treatment part, which is separated from the biological treatment part by a third partition wall and communicates with the lower end of the wastewater descending path; and the sludge sedimentation part Treated water after passing A process-water riser passage for raising the, having the biological treatment process water riser passage that is separated by a fourth partition wall with respect to unit, but according to the biological treatment tank.

【0007】[0007]

【実施例】図1は、本発明の実施例に係る生物処理槽を
示す概略図である。以下、この装置について、主として
廃水の流れに従って説明する。
EXAMPLE FIG. 1 is a schematic view showing a biological treatment tank according to an example of the present invention. Hereinafter, this apparatus will be described mainly according to the flow of wastewater.

【0008】タンク1内は、大体において、生物処理部
10、廃水上昇路11、廃水下降路12、汚泥沈澱部13及び処
理水上昇路15に区分されている。まず、タンク1の上部
側には、例えば円筒形状をなす生物処理部10が設けら
れ、この生物処理部10へと矢印Aのように廃水が注入さ
れる。生物処理部10においては、好気性微生物を含有す
る活性汚泥が廃水に混合され、廃水内の有機物が生物処
理される。生物処理部10の底部には、廃水へと空気を吹
き込むための散気装置8が設置されている。
The inside of the tank 1 is generally a biological treatment section.
It is divided into 10, a wastewater rising path 11, a wastewater descending path 12, a sludge settling section 13 and a treated water rising path 15. First, a biological treatment unit 10 having, for example, a cylindrical shape is provided on the upper side of the tank 1, and waste water is injected into the biological treatment unit 10 as indicated by an arrow A. In the biological treatment unit 10, activated sludge containing aerobic microorganisms is mixed with wastewater, and organic matter in the wastewater is biologically treated. At the bottom of the biological treatment unit 10, an air diffuser 8 for blowing air into wastewater is installed.

【0009】生物処理部10内を矢印Bのように流れた廃
水は、次いで廃水上昇路11内を上昇する。この廃水上昇
路11は生物処理部10の内側に設けられ、これと第一の隔
壁4によって区分される。
The wastewater flowing in the biological treatment section 10 as shown by the arrow B then rises in the wastewater rising path 11. This wastewater ascending path 11 is provided inside the biological treatment section 10 and is divided by this and the first partition wall 4.

【0010】次いで、廃水上昇路11内を上昇した廃水
は、廃水上昇路11の上端に達すると、矢印Cのように第
二の隔壁5を越流し、廃水下降路12内を下降する。廃水
上昇路11と廃水下降路12とは第二の隔壁5によって区分
される。
Next, when the wastewater that has risen in the wastewater rise passage 11 reaches the upper end of the wastewater rise passage 11, it overflows the second partition wall 5 as shown by arrow C and descends in the wastewater fall passage 12. The wastewater ascending path 11 and the wastewater descending path 12 are divided by the second partition wall 5.

【0011】生物処理部10、廃水上昇路11及び廃水下降
路12の下方には、汚泥沈澱部13が形成されている。そし
て、生物処理部10及び廃水上昇路11と汚泥沈澱部13とは
互いに第三の隔壁9によって隔離され、直接の廃水の流
通が阻止されている。また、廃水下降路12の下端が汚
泥沈澱部13と連通しており、廃水下降路12を流下し
てきた廃水が汚泥沈澱部13内へと流入する。更に、第二
の隔壁5の下端には、第三の隔壁9を越えて延在部5aが
形成されている。
A sludge settling section 13 is formed below the biological treatment section 10, the wastewater rising path 11 and the wastewater descending path 12. Then, the biological treatment unit 10, the wastewater rising path 11, and the sludge settling unit 13 are isolated from each other by the third partition wall 9, and direct circulation of the wastewater is blocked. Further, the lower end of the wastewater descending path 12 communicates with the sludge settling section 13, and the wastewater flowing down the wastewater descending section 12 flows into the sludge settling section 13. Further, an extension portion 5a is formed at the lower end of the second partition wall 5 beyond the third partition wall 9.

【0012】汚泥沈澱部13内に汚泥掻寄機6が設置さ
れ、またタンク1の底部からは、随時矢印Fのように汚
泥を抜く。
A sludge scraper 6 is installed in the sludge settling section 13, and sludge is removed from the bottom of the tank 1 at any time as indicated by arrow F.

【0013】生物処理部10の外側には、第四の隔壁2を
隔てて処理水上昇路15が設けられており、処理水上昇路
15の下端は汚泥沈澱部13の外周部に連通している。従っ
て、廃水下降路12内を流下してきた廃水は、矢印Dのよ
うに汚泥沈澱部13内を通過し、最終的に汚泥から分離さ
れた処理水が処理水上昇路15内を上昇し、矢印Eのよう
に越流して処理水受け部1aに入り、ここから矢印Hのよ
うに排出、例えば放流される。
A treated water rising path 15 is provided outside the biological treatment section 10 with a fourth partition wall 2 interposed therebetween.
The lower end of 15 communicates with the outer periphery of the sludge settling section 13. Therefore, the wastewater flowing down in the wastewater descending path 12 passes through the sludge settling section 13 as shown by an arrow D, and the treated water separated from the sludge finally rises in the treated water ascending path 15, As shown by E, the overflowed water enters the treated water receiving portion 1a, from which it is discharged as shown by arrow H, for example, discharged.

【0014】第四の隔壁2の下端には、第三の隔壁9と
の接合位置から更に下方へと伸びるスカート2aが形成さ
れる。そして、第三の隔壁9には、一箇所又は二箇所以
上の逆止弁付ガス抜き3が設けられる。なお、図中7は
水位面である。
A skirt 2a is formed at the lower end of the fourth partition 2 and extends further downward from the position where the third partition 9 is joined. The third partition wall 9 is provided with one or more gas vents 3 with check valves. In addition, 7 in the figure is a water level surface.

【0015】本実施例に係る生物処理槽によれば、生物
処理部10と汚泥沈澱部13とが第三の隔壁9によって隔離
され、これにより両者の間で廃水の直接の交流が阻止さ
れているので、汚泥沈澱部13内に沈積した汚泥を生物処
理部10へと巻き上げることがなくなり、従って、汚泥沈
澱効率を向上させることができる。
According to the biological treatment tank of this embodiment, the biological treatment section 10 and the sludge settling section 13 are separated by the third partition wall 9, whereby direct exchange of wastewater between them is blocked. Since the sludge settled in the sludge settling section 13 is not rolled up to the biological treatment section 10, the sludge settling efficiency can be improved.

【0016】また、第一の隔壁4を設けて廃水上昇路11
及び廃水下降路12を形成し、生物処理後の廃水を上昇、
下降させて汚濁沈澱槽へと送り込んでいるので、生物処
理部10内への汚泥返送を廃止し、またはこの返送量をご
く少量にしても、廃水の処理を行える。
Further, the first partition wall 4 is provided so that the wastewater rising path 11
And forming a wastewater descending path 12 to raise the wastewater after biological treatment,
Since it is lowered and sent to the pollutant sedimentation tank, wastewater can be treated even if sludge return to the biological treatment section 10 is abolished, or even if this return amount is very small.

【0017】更に、第四の隔壁2の下端にスカート2aを
設けているので、汚泥の腐敗ガス等の各種ガスが汚泥沈
澱部13の上部空間20に集合する。従って、上部空間20に
集合したガスを逆止弁付ガス抜き3から抜くことで、汚
泥沈澱部13内のガス抜きを有効に行えるので、このガス
によって処理水上昇路15中へと汚泥が浮上してくる事態
を防止できる。
Further, since the skirt 2a is provided at the lower end of the fourth partition wall 2, various gases such as sludge decay gas gather in the upper space 20 of the sludge settling section 13. Therefore, the gas collected in the upper space 20 can be effectively discharged from the sludge settling section 13 by removing the gas from the degasser 3 with a check valve, so that the sludge floats up into the treated water rising path 15. You can prevent the coming situation.

【0018】しかも、第二の隔壁5の下端に延在部5aを
設けているので、この延在部5aがない場合に比較して、
廃水を汚泥沈澱部13の一層深い領域へと送り込むことが
できるので、廃水中に含まれる水が処理水上昇路15の下
端部へと至るまでの汚泥中の通過距離、即ち濾過距離が
長い、従って、処理水の汚泥からの分離を一層促進する
ことができる。また、同じ理由から、タンク1全体を小
型化しても上記濾過距離をある程度長くすることができ
る。
Moreover, since the extending portion 5a is provided at the lower end of the second partition wall 5, as compared with the case where this extending portion 5a is not provided,
Since the wastewater can be sent to a deeper region of the sludge settling section 13, the water contained in the wastewater passes through the sludge to the lower end of the treated water ascending path 15, that is, the filtration distance is long, Therefore, separation of treated water from sludge can be further promoted. For the same reason, the filtration distance can be increased to some extent even if the entire tank 1 is downsized.

【0019】以上の結果より、従来よりも清浄な処理水
を得ることが可能であり、また従来の処理装置に比べて
処理効率の向上を図ると共に、これによって廃水処理装
置の設置面積を小さくすることも可能となる。
From the above results, it is possible to obtain treated water that is cleaner than the conventional one, and to improve the treatment efficiency as compared with the conventional treatment equipment, thereby reducing the installation area of the wastewater treatment equipment. It is also possible.

【0020】以下、図1及び図2に示す廃水処理装置を
それぞれ用い、廃水処理実験を行った。原廃水の性状は
BOD 100〜150mg/l 、SS 150〜200mg/l であった。この
原廃水を同規模の図1及び図2の廃水処理装置へと供給
し、運転した。その結果、処理水の性状は以下の通りで
あった。
Hereinafter, wastewater treatment experiments were conducted using the wastewater treatment devices shown in FIGS. 1 and 2, respectively. Raw wastewater properties
The BOD was 100 to 150 mg / l and the SS was 150 to 200 mg / l. This raw wastewater was supplied to the wastewater treatment apparatus of the same scale shown in FIGS. 1 and 2 and operated. As a result, the properties of the treated water were as follows.

【0021】[0021]

【発明の効果】本発明に係る生物処理槽によれば、生物
処理部と汚泥沈澱部とが第三の隔壁によって隔離され、
これにより両者の間で廃水の直接の交流が阻止されてい
るので、汚泥沈澱部内に沈積した汚泥を生物処理部へと
巻き上げることがなくなり、従って、汚濁沈澱効率を向
上させることができる。
According to the biological treatment tank of the present invention, the biological treatment section and the sludge settling section are separated by the third partition wall,
As a result, direct interaction between the wastewater is prevented between the two, so that sludge accumulated in the sludge settling section is not rolled up to the biological treatment section, and therefore the pollution settling efficiency can be improved.

【0022】また、第一の隔壁によって生物処理部と区
分された廃水上昇路を設け、生物処理後の廃水をこの廃
水上昇路内で上昇させ、次いで廃水上昇路の上端へと上
昇した廃水を下降させて汚泥沈澱部へと送るので、生物
処理部内への汚泥返送を廃止し、またはこの返送量をご
く少量にしても、廃水の生物処理を行える。
Further, a wastewater rising path separated from the biological treatment section by the first partition is provided, the wastewater after the biological treatment is raised in this wastewater rising path, and then the wastewater rising to the upper end of the wastewater rising path is discharged. Since it is lowered and sent to the sludge settling section, the biological treatment of wastewater can be carried out even if sludge return to the biological treatment section is abolished or even if the returned amount is very small.

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

【図1】本発明の実施例に係る生物処理槽を示す概略図
である。
FIG. 1 is a schematic view showing a biological treatment tank according to an embodiment of the present invention.

【図2】従来例に係る生物処理槽を示す概略図である。FIG. 2 is a schematic view showing a biological treatment tank according to a conventional example.

【符号の説明】[Explanation of symbols]

1,21 タンク 1a, 21a 処理水受け部 2 第四の隔壁 2a 第四の隔壁の下端に延在するスカート 3 逆止弁付ガス抜き 4 第一の隔壁 5 第二の隔壁 5a 第二の隔壁の下端の延在部 6 汚泥掻寄機 7 水位 8 散気装置 9 生物処理部と汚泥沈澱部とを隔離する第三の隔壁 10 生物処理部 11 廃水上昇路 12 廃水下降路 13 汚泥沈澱部 15 処理水上昇路 20 汚泥沈澱部の上部空間 A,B,C,D 廃水の流れ E,G,H 汚泥に対して分離された処理水の流れ F 汚泥抜き 1,21 Tanks 1a, 21a Treated water receiving part 2 Fourth partition 2a Skirt extending to the lower end of the fourth partition 3 Gas vent with check valve 4 First partition 5 Second partition 5a Second partition Extension part at the lower end of the tank 6 Sludge attractor 7 Water level 8 Air diffuser 9 Third partition wall separating the biological treatment section and the sludge sedimentation section 10 Biological treatment section 11 Wastewater ascending path 12 Wastewater descending path 13 Sludge sedimentation section 15 Treated water rising path 20 Upper space of sludge settling area A, B, C, D Wastewater flow E, G, H Flow of treated water separated from sludge F F Sludge removal

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 好気性微生物を含有する活性汚泥と、生
物処理部内へ流入する廃水とを混合し、この廃水内の有
機物を生物処理する生物処理部;前記廃水へと空気を吹
き込むために、前記生物処理部内に配置された散気装
置;前記生物処理部に対して第一の隔壁によって区分さ
れた廃水上昇路であって、前記生物処理後の廃水を上昇
させるための廃水上昇路;この廃水上昇路に対して第二
の隔壁によって区分された廃水下降路であって、この廃
水上昇路の上端へと上昇した廃水を下降させるための廃
水下降路;前記生物処理部の下方に形成された汚泥沈澱
部であって、前記生物処理部に対して第三の隔壁によっ
て隔離され、前記廃水下降路の下端と連通する汚泥沈澱
部;及びこの汚泥沈澱部を通過した後の処理水を上昇さ
せるための処理水上昇路であって、前記生物処理部に対
して第四の隔壁によって隔離された処理水上昇路を有す
る、生物処理槽。
1. A biological treatment unit for mixing activated sludge containing aerobic microorganisms with wastewater flowing into the biological treatment unit and biologically treating organic matter in the wastewater; for blowing air into the wastewater, An air diffuser disposed in the biological treatment section; a wastewater rising path divided by the first partition wall with respect to the biological processing section, for raising the wastewater after the biological processing; A wastewater descending passage divided by a second partition wall with respect to the wastewater rising passage, the wastewater descending passage for descending the wastewater rising to the upper end of the wastewater rising passage; formed below the biological treatment section A sludge sedimentation part, which is isolated from the biological treatment part by a third partition wall and communicates with the lower end of the wastewater descending path; and the treated water after passing through the sludge sedimentation part is raised. Increased treated water to allow A biological treatment tank having a treated water rising passage isolated from the biological treatment section by a fourth partition.
JP2411972A 1990-12-20 1990-12-20 Biological treatment tank Expired - Fee Related JPH0673678B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2411972A JPH0673678B2 (en) 1990-12-20 1990-12-20 Biological treatment tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2411972A JPH0673678B2 (en) 1990-12-20 1990-12-20 Biological treatment tank

Publications (2)

Publication Number Publication Date
JPH04222695A JPH04222695A (en) 1992-08-12
JPH0673678B2 true JPH0673678B2 (en) 1994-09-21

Family

ID=18520878

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2411972A Expired - Fee Related JPH0673678B2 (en) 1990-12-20 1990-12-20 Biological treatment tank

Country Status (1)

Country Link
JP (1) JPH0673678B2 (en)

Also Published As

Publication number Publication date
JPH04222695A (en) 1992-08-12

Similar Documents

Publication Publication Date Title
US4082671A (en) Sludge thickening apparatus
KR890004193B1 (en) Apparatus for biological purification of waste water by using submerged filter
US2360812A (en) Purification of liquids
JPS6359760B2 (en)
US3735870A (en) Activated sludge plant
JP2008502472A (en) Water treatment process and apparatus by fluid flow
US6719911B2 (en) Apparatus and method for the treatment of a contaminated fluid
JP2938191B2 (en) Activated sludge degassing method and apparatus
US4173534A (en) Sludge thickening apparatus and process
JPH0673678B2 (en) Biological treatment tank
KR100628481B1 (en) Plant and process for wastewater treatment
JP2000354858A (en) Sewage treatment method and device therefor
US6837997B2 (en) Disposal of sediment from pond or lagoon at petroleum refinery
JPH09225491A (en) Anaerobic treating device of organic waste water
JPH04131185A (en) Electric floating device
CN218709814U (en) Oily wastewater treatment system
KR0134918B1 (en) Water purification apparatus
JPH05301005A (en) Precipitation tank for advanced wastewater treatment
RU2769593C1 (en) Apparatus for mechanical and biological purification of household waste water and method for use thereof
JPS6143118B2 (en)
CN208649043U (en) A kind of petroleum wastewater oily-water seperating equipment
JPS6017280Y2 (en) Sewage purification equipment
KR200251956Y1 (en) Contact filter container sewage septic tank for providing with flow tank having three stages processing progress
JPS56121689A (en) Fluid bed type wastewater treating apparatus
JPS6274489A (en) Recirculation aeration type sewage treatment apparatus

Legal Events

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