JPH04222695A - Biological treating tank - Google Patents
Biological treating tankInfo
- Publication number
- JPH04222695A JPH04222695A JP2411972A JP41197290A JPH04222695A JP H04222695 A JPH04222695 A JP H04222695A JP 2411972 A JP2411972 A JP 2411972A JP 41197290 A JP41197290 A JP 41197290A JP H04222695 A JPH04222695 A JP H04222695A
- Authority
- JP
- Japan
- Prior art keywords
- wastewater
- biological treatment
- sludge
- section
- waste liquid
- 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.)
- Granted
Links
- 239000010802 sludge Substances 0.000 claims abstract description 70
- 238000005192 partition Methods 0.000 claims abstract description 36
- 239000005416 organic matter Substances 0.000 claims abstract description 4
- 239000002351 wastewater Substances 0.000 claims description 67
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 30
- 230000001174 ascending effect Effects 0.000 claims description 19
- 230000000630 rising effect Effects 0.000 claims description 10
- 238000005273 aeration Methods 0.000 claims description 6
- 244000005700 microbiome Species 0.000 claims description 6
- 238000004062 sedimentation Methods 0.000 abstract description 4
- 238000000926 separation method Methods 0.000 abstract description 2
- 239000007788 liquid Substances 0.000 abstract 10
- 239000002699 waste material Substances 0.000 abstract 9
- 239000007789 gas Substances 0.000 description 8
- 239000010865 sewage Substances 0.000 description 6
- 238000004065 wastewater treatment Methods 0.000 description 5
- 238000010586 diagram Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 231100000719 pollutant Toxicity 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
Abstract
Description
【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。BACKGROUND OF THE INVENTION The so-called activated sludge method is known as a method of separating and removing pollutant components in sewage and converting the sewage into clear and safe water. In this system, activated sludge mainly composed of microorganisms is mixed with sewage flowing into an aeration tank, and compressed air is injected from the bottom in the form of bubbles. In this way, the sewage and activated sludge are mixed and stirred, and the activity of aerobic microorganisms in the activated sludge is increased by oxygen in the air, resulting in floating,
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21
a 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。[0003] 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 inside the tank 21, and the inside of the tank 21 is generally divided into a biological treatment section 10, a sludge settling section 13, and a treated water ascending passage 15 by this partition wall 22. Then, the wastewater such as sewage is transferred to the biological treatment section 10 as shown by arrow A.
This wastewater is mixed with activated sludge and
Air is supplied from an aeration device 8 installed at the bottom of the biological treatment section 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 in the treated water ascending path 15 as shown by arrow G. After that, the treated water that has reached the water level 7 is transferred to the treated water receiving part 21.
a, and is discharged outside the device as shown by arrow H. Sludge is removed from the bottom of the tank 21 at any time as indicated by arrow F. In addition, 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1
0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。[Problems to be Solved by the Invention] However, in the apparatus shown in FIG.
The sludge sedimentation efficiency decreases. Furthermore, 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。[0005] An object of the present invention is to improve the sludge settling efficiency by preventing the sludge deposited in the sludge settling section from being rolled up, and to eliminate the need for returning activated sludge to the biological treatment tank or to minimize the need for returning activated sludge to the biological treatment tank. The objective is to provide a wastewater treatment device that can
【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。[Means for Solving the Problems] The present invention provides a biological treatment section that mixes activated sludge containing aerobic microorganisms with wastewater flowing into the biological treatment section, and biologically treats organic matter in this wastewater; an air diffuser disposed within the biological treatment section for blowing air into the biological treatment section; a wastewater rise path separated from the biological treatment section by a first partition wall, which raises the wastewater after the biological treatment; a wastewater descending path separated from the wastewater ascending path by a second partition wall for lowering the wastewater that has risen to the upper end of the wastewater ascending path; a sludge settling section formed below the biological treatment section, the sludge settling section being isolated from the biological treatment section by a third partition and communicating with the lower end of the wastewater descending path; The present invention relates to a biological treatment tank having a treated water rising path for raising the treated water after passing through the biological treatment section, the treated water rising path being isolated from the biological treatment section by a fourth partition.
【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。Embodiment FIG. 1 is a schematic diagram showing a biological treatment tank according to an embodiment of the present invention. This device will be explained below 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1
3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1
0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。Inside the tank 1, there are generally a biological treatment section 10, a wastewater ascending passage 11, a wastewater descending passage 12, and a sludge settling section 1.
3 and a treated water rising path 15. First, on the upper side of the tank 1, there is a biological treatment section 1 having a cylindrical shape, for example.
0 is provided, and wastewater is injected into this biological treatment section 10 as shown by arrow A. In the biological treatment section 10, activated sludge containing aerobic microorganisms is mixed with wastewater, and organic matter in the wastewater is subjected to biological treatment. At the bottom of the biological treatment section 10,
An air diffuser 8 is installed to blow air into the wastewater.
【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。[0009] The wastewater flowing in the biological treatment section 10 as shown by arrow B then rises in the wastewater ascending path 11. This wastewater ascending path 11 is provided inside the biological treatment section 10 and is separated from this by 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 rising in the wastewater ascending passage 11 reaches the upper end of the wastewater ascending passage 11, it flows over the second partition wall 5 as shown by arrow C and descends within the wastewater descending passage 12. The wastewater ascending passage 11 and the wastewater descending passage 12 are separated by a 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 ascending passage 11, and the wastewater descending passage 12. The biological treatment section 10, the wastewater ascending path 11, and the sludge settling section 13 are separated from each other by a third partition wall 9,
Direct wastewater flow is blocked. Further, the lower end of the wastewater descending passage 12 communicates with the sludge settling section 13 , and the wastewater flowing down the wastewater descending passage 12 flows into the sludge settling section 13 . Furthermore, an extending portion 5 a is formed at the lower end of the second partition 5 so as to extend beyond the third partition 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 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 fourth partition wall 2 is provided on the outside of the biological treatment section 10.
A treated water rising path 15 is provided across the sludge settling section 13, and the lower end of the treated water rising path 15 communicates with the outer peripheral portion of the sludge settling section 13. Therefore, the wastewater flowing down inside the wastewater descending path 12 is
The treated water passes through the sludge settling part 13 as shown by arrow D, and is finally separated from the sludge. The treated water rises in the treated water rising path 15, and then overflows as shown by arrow E and enters the treated water receiving part 1a. , from which it is discharged, for example, discharged as shown by arrow H.
【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 wall 2 and extends further downward from the joining position with the third partition wall 9. The third partition wall 9 is provided with one or more gas vents 3 with check valves. In addition, 7 in the figure
is the water level.
【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 according to this embodiment, the biological treatment section 10 and the sludge settling section 13 are separated by the third partition wall 9, thereby preventing direct exchange of wastewater between them. Therefore, the sludge deposited in the sludge settling section 13 is not rolled up to the biological treatment section 10, and therefore, 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1
1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。[0016] Furthermore, a first partition wall 4 is provided to separate the wastewater ascending path 1.
1 and wastewater descending path 12 are formed, and the wastewater after biological treatment is raised and lowered and sent to the pollution sedimentation tank, so the return of sludge to the biological treatment section 10 can be abolished or the amount of this return can be minimized. Wastewater can be treated even in small quantities.
【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。Furthermore, a skirt 2a is provided at the lower end of the fourth partition wall 2.
, various gases such as sludge putrefaction gas gather in the upper space 20 of the sludge settling section 13. Therefore, by removing the gas collected in the upper space 20 from the gas vent 3 equipped with a check valve, the gas in the sludge settling section 13 can be effectively vented, and this gas causes the sludge to float into the treated water ascending path 15. You can prevent this from happening.
【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, an extending portion 5a is provided at the lower end of the second partition wall 5.
is provided, the wastewater can be sent into a deeper region of the sludge settling section 13 compared to the case where the extension section 5a is not provided. The passage distance through the sludge to reach the lower end, that is, the filtration distance is long, so separation of the treated water from the sludge can be further promoted. Also, for the same reason, tank 1
Even if the entire device is downsized, the filtration distance can be increased to some extent.
【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。[0019] From the above results, it is possible to obtain treated water that is cleaner than before, and the treatment efficiency is improved compared to conventional treatment equipment, and the installation area of the wastewater treatment equipment is thereby reduced. It also becomes 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。[0020] Below, wastewater treatment experiments were conducted using the wastewater treatment apparatuses shown in FIGS. 1 and 2, respectively. The properties of the raw wastewater are BOD 100~150mg/l, SS 150~
It was 200mg/l. Figure 1 shows the same scale of this raw wastewater.
and supplied to the wastewater treatment equipment shown in Figure 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。[Effects of the Invention] According to the biological treatment tank according to the present invention, the biological treatment section and the sludge settling section are separated by the third partition wall,
Since this prevents direct exchange of wastewater between the two, the sludge deposited in the sludge settling section is not rolled up to the biological treatment section, and therefore the sludge 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。[0022] Furthermore, a wastewater ascending passage separated from the biological treatment section by the first partition wall is provided, and the wastewater after biological treatment is allowed to rise within this wastewater ascending passage, and then the wastewater that has risen to the upper end of the wastewater ascending passage is discharged. Since the sludge is lowered and sent to the sludge settling section, biological treatment of wastewater can be performed even if the sludge is not returned to the biological treatment section or the amount of sludge returned is reduced to a very small amount.
【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 diagram 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 diagram showing a biological treatment tank according to a conventional example.
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 section 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 Extended portion at the lower end 6 Sludge scraper 7 Water level 8 Aeration device 9 Third partition wall 10 separating the biological treatment section and sludge settling section Biological treatment section 11 Wastewater ascending passage 12 Wastewater descending passage 13 Sludge settling section 15 Treated water rising path 20 Upper space of sludge settling section A, B, C, D Wastewater flow E, G, H Treated water flow separated from sludge F
Sludge removal
Claims (1)
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。[Claim 1] Activated sludge containing aerobic microorganisms;
A biological treatment unit that mixes wastewater flowing into the biological treatment unit and biologically treats organic matter in the wastewater; an aeration device disposed within the biological treatment unit to blow air into the wastewater; the biological treatment unit; a wastewater riseway for raising the wastewater after the biological treatment, the wastewater riseway being separated by a first partition wall from the wastewater riseway; A descending path for lowering the wastewater that has risen to the upper end of the wastewater ascending path; a sludge settling section formed below the biological treatment section; a sludge settling section separated by a third partition wall and communicating with the lower end of the wastewater descending channel; and a treated water rising channel for raising the treated water after passing through the sludge settling section, the biological treatment section A biological treatment tank having a treated water rising path separated from the water by a fourth partition wall.
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 true JPH04222695A (en) | 1992-08-12 |
JPH0673678B2 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) |
-
1990
- 1990-12-20 JP JP2411972A patent/JPH0673678B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPH0673678B2 (en) | 1994-09-21 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP5749731B2 (en) | Sewage treatment equipment | |
US4082671A (en) | Sludge thickening apparatus | |
JPS6359760B2 (en) | ||
SU1358783A3 (en) | Device for biological treatment of waste water | |
US6719911B2 (en) | Apparatus and method for the treatment of a contaminated fluid | |
US4265753A (en) | Aeration filtration tank and water treatment system | |
JP2000117285A (en) | Anaerobic treatment device for organic wastewater | |
US4173534A (en) | Sludge thickening apparatus and process | |
JP3150530B2 (en) | Biological nitrogen removal equipment | |
JPH04222695A (en) | Biological treating tank | |
KR20040064579A (en) | Fluids fluxion process and plant for wastewater treatment | |
US4306969A (en) | Apparatus for sewage purification | |
JPS6351994A (en) | System for treating drainage | |
KR101106761B1 (en) | Separator circulation type activated sludge aeration tank and water treatment method using the same | |
CN219950701U (en) | Self-circulation device of AO sewage treatment equipment | |
KR100368176B1 (en) | Wastewater disposal device | |
KR102545064B1 (en) | Multi-stage sewage treatment system | |
JPH09225491A (en) | Anaerobic treating device of organic waste water | |
CN113929208B (en) | Stage type circulating biochemical aeration process applied to water treatment | |
CN218709814U (en) | Oily wastewater treatment system | |
RU2769593C1 (en) | Apparatus for mechanical and biological purification of household waste water and method for use thereof | |
JPH1094794A (en) | Organic waste water anaerobic treatment device | |
CN215756921U (en) | Air-lift circulation reaction device | |
JPS6274489A (en) | Recirculation aeration type sewage treatment apparatus | |
KR101992386B1 (en) | Wastewater treatment system with improved efficiency of separation of precipitated matter and removing of floating matter and scum |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
LAPS | Cancellation because of no payment of annual fees |