JPS6350077B2 - - Google Patents
Info
- Publication number
- JPS6350077B2 JPS6350077B2 JP59129009A JP12900984A JPS6350077B2 JP S6350077 B2 JPS6350077 B2 JP S6350077B2 JP 59129009 A JP59129009 A JP 59129009A JP 12900984 A JP12900984 A JP 12900984A JP S6350077 B2 JPS6350077 B2 JP S6350077B2
- Authority
- JP
- Japan
- Prior art keywords
- liquid
- scum
- water level
- aeration
- treatment tank
- 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
- 239000007788 liquid Substances 0.000 claims description 44
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 30
- 238000005273 aeration Methods 0.000 claims description 24
- 238000000034 method Methods 0.000 claims description 23
- 239000006228 supernatant Substances 0.000 claims description 18
- 239000010802 sludge Substances 0.000 claims description 9
- 238000001556 precipitation Methods 0.000 claims description 4
- 238000010992 reflux Methods 0.000 claims description 2
- 239000000203 mixture Substances 0.000 description 6
- 239000010865 sewage Substances 0.000 description 6
- 239000002351 wastewater Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 238000007599 discharging Methods 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 238000005276 aerator Methods 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 238000010008 shearing Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000003756 stirring 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
- Activated Sludge Processes (AREA)
- Removal Of Floating Material (AREA)
Description
この発明はスカムを効果的に排出除去できる回
分式の汚水処理装置に関する。
The present invention relates to a batch-type sewage treatment device that can effectively discharge and remove scum.
従来、1つの槽内で曝気・沈殿・上澄液の放流
を行う回分式活性汚泥処理装置においては、沈殿
工程の後、沈殿上澄液を排出するが、この時、処
理槽内にはスカムが浮上している場合が多くあ
る。
そして、上澄液の放流は液面上を上下動する上
澄液排出手段によつて行うが、この際、通常この
上澄液排出手段のうち溢流管を囲繞するスカムバ
ツフルによつてスカムの混入を防止している。
しかし、従来のものでは、スカムバツフルが水
面上に下降した時点で、スカムバツフル内にある
スカムはどうしても上澄液排出手段のうちの溢流
管に流入し放流されてしまい、またスカムの分
離、排除を行えないという問題点があつた。ま
た、槽内水位が変化するため独立したスカム排出
機構を作るのが難しいという問題点もあつた。
Conventionally, in batch-type activated sludge treatment equipment that performs aeration, precipitation, and discharge of supernatant liquid in one tank, the precipitated supernatant liquid is discharged after the sedimentation process, but at this time, scum remains in the treatment tank. are often emerging. The supernatant liquid is discharged by a supernatant liquid discharge means that moves up and down above the liquid surface. At this time, the scum is usually removed by a scum baffle surrounding the overflow pipe of the supernatant liquid discharge means. Prevents contamination. However, with conventional systems, when the scum bathful descends to the water surface, the scum inside the scum bathtubule inevitably flows into the overflow pipe of the supernatant liquid discharge means and is discharged, and it is difficult to separate and remove the scum. There was a problem that I couldn't do it. Another problem was that it was difficult to create an independent scum discharge mechanism because the water level in the tank changed.
この発明は上記問題点を解消するためになされ
たもので、曝気工程時に気液混合液の噴出により
曝気を行う曝気装置で放流工程の終了後所定時間
にわたり液だけを噴出させることにより、上記放
流工程で水位が低下した処理槽内に水平還流方向
への汚水循環流を生起させ、この循環流で汚水中
のスカムを、上記処理槽内の低水位より上方の平
均水位付近に設置されたスキマー方向に移流させ
て該スキマーに流入させることによつて、上記ス
カムを効果的に排除できるようした汚水処理装置
を提供することを目的とする。
This invention has been made in order to solve the above-mentioned problems.The aeration device that performs aeration by spouting a gas-liquid mixture during the aeration process sprays out only the liquid for a predetermined period of time after the discharge process is completed, thereby eliminating the above-mentioned discharge. A sewage circulation flow is generated in the horizontal return direction in the treatment tank whose water level has decreased during the process, and this circulation flow removes scum from the wastewater using a skimmer installed near the average water level above the low water level in the treatment tank. It is an object of the present invention to provide a sewage treatment device that can effectively eliminate the scum by advecting the scum in the direction of the scum and flowing it into the skimmer.
以下、この発明の一実施例について図面を参照
して説明する。
第1図、第2図に示すように回分式活性汚泥処
理槽1には、上澄液排出手段2と、スカム排出用
のスキマー3と、曝気工程時に気泡混合液の噴出
により曝気を行い、放流工程終了後所定時間にわ
たり液だけを噴出させる曝気装置(ジエツトエア
レータ)4とが配置されている。
上記上澄液排出手段2は、第2図に示すよう
に、沈殿工程に続く放流工程時に上澄液を排出す
るものであつて、軸パイプ5を軸心として上下回
動可能に支持された排出パイプ6と、この排出パ
イプ6の自由端に取付けられ、溢流口7aが開口
された溢流管7と、フロート8とで構成されてい
る。従つて、溢流管7が上記処理槽1内の高水位
(H.W.L)から低水位(L.W.L)まで下降してい
る状態では、処理槽1内の上澄液は上澄液排出手
段2の溢流口7aより溢流管7内へ流入し、軸パ
イプ5を経て外部へ放流される。また、図示しな
い回動手段によつて溢流管7が高水位液面より高
い位置になるように回動変位された状態では、処
理槽1内の液体の放流は行われない。
ここで、上記スカム排出用のスキマー3は、上
記処理槽1内の平均水位付近、更に詳しくは第2
図において、低水位(L.W.L)より上方の平均水
位(M.W.L)付近で上記処理槽1内を横断する
方向に水平に配置され、上記低水位より上方の平
均水位で開口するスカム排出口3aを有してい
る。なお、上記スキマー3は、低水位(L.W.L)
と高水位(H.W.L)との間の平均水位(M.W.L)
付近であれば、そのどこに設置してもよい。
かかるスキマー3には、第1図に示すように、
放流工程終了後の所定時間にのみ開放されるスカ
ム排出弁9が接続されている。
上記曝気装置4は、液のみの噴出により上記処
理槽1内で矢印方向(還流方向)の循環流を生起
させると共に曝気工程時に気液混合液の噴出によ
り曝気を行うものであつて、循環ポンプ10と、
切換制御する曝気ブロア11とで構成され、気液
混合液の噴出、即ちジエツト流の剪断作用や周辺
流の巻き込み作用によつて小さな動力で充分な撹
拌混合効果を奏する。
ここで、上記曝気工程では、循環ポンプ10お
よび曝気ブロア11の双方を運転し、気液混合液
を噴出する。しかし、放流工程終了後の所定時間
において、スカムをスキマー3方向に移流させる
時には気液混合を必要としないので、循環ポンプ
10のみを作動させ、矢印方向の循環流のみを生
起させる。この所定時間はタイマで設定しても、
槽内水位で設定してもよい。
次に、この発明の作用を説明する。
処理槽1内では、曝気装置4からの気液混合液
の噴出によつて矢印方向の循環流を生起させなが
ら流入する汚水の曝気を行う曝気工程と、空気の
吹込みを中止して液体中の活性汚泥を沈殿させる
沈殿工程と、上澄液排出手段2を下降させて、上
澄液を排出する放流工程を1サイクルとする操作
を繰返し、連続的もしくは任意的に流入口1aか
ら供給される流入汚水を活性汚泥と混合させ処理
する。また、処理槽1内の汚泥は適当な時間を選
んで引抜かれる。
ここで、放流工程が終了した時、液面は低水位
であると共に流入口1aから新たな汚水が流入し
てくる。これとほぼ同時に曝気装置4の循環ポン
プ10のみが作動し、液のみが噴出されて循環流
が生起されることにより、この循環流によつて、
スカムが第1図中の矢印方向に移流され、第2図
に示すようにスキマー3のスカム排出口3a近傍
に集められる。そして、順次、流入してくる汚水
によつて、上記処理槽1内の水位が徐々に上昇し
ていき、槽内液面が低水位より上方の平均水位付
近に達すると、図示しない制御装置によつて制御
されたスカム排出弁9が閉状態から開状態とな
り、スカムは流入汚水と共に処理槽1外へ排出さ
れる。
この場合、液面が平均水位付近に達するまで、
スカムは曝気装置4の液のみの噴出による循環流
により処理槽1内を循環することになる。このた
め、低水位から平均水位付近に到達するまでの時
間を調べタイマ設定で遅らすことにより、スカム
が処理槽1内を循環する時間を少なくすることが
できる。そして、所定時間(例えば3〜5分程
度)経過後、スカム排出弁9は閉じられ、スカム
排出が終了すると共に、新たに曝気工程が開始つ
される。なお、スカム排出弁9は、上澄液排出手
段2が低水位に達し、上澄液排出手段2の下降が
停止される時の信号で開いてもよい。こうすれ
ば、平均水位付近の検知は必要ない。また、スカ
ムの放流は毎回行わず必要に応じて行つてもよ
い。
An embodiment of the present invention will be described below with reference to the drawings. As shown in FIGS. 1 and 2, the batch type activated sludge treatment tank 1 includes a supernatant liquid discharge means 2, a skimmer 3 for scum discharge, and aeration is performed by jetting out a bubble mixture during the aeration process. An aeration device (jet aerator) 4 is arranged to jet out only the liquid for a predetermined period of time after the discharge process is completed. As shown in FIG. 2, the supernatant liquid discharge means 2 is for discharging the supernatant liquid during the discharge process following the precipitation process, and is supported so as to be movable up and down about a shaft pipe 5. It consists of a discharge pipe 6, an overflow pipe 7 attached to the free end of the discharge pipe 6 and having an overflow port 7a, and a float 8. Therefore, when the overflow pipe 7 is descending from the high water level (HWL) in the treatment tank 1 to the low water level (LWL), the supernatant liquid in the treatment tank 1 is discharged from the overflow of the supernatant liquid discharge means 2. It flows into the overflow pipe 7 from the flow port 7a, and is discharged to the outside through the shaft pipe 5. Further, in a state where the overflow pipe 7 is rotated and displaced by a rotation means (not shown) so that it is at a position higher than the high water level liquid level, the liquid in the processing tank 1 is not discharged. Here, the skimmer 3 for scum discharge is operated near the average water level in the treatment tank 1, more specifically at the second
In the figure, a scum outlet 3a is arranged horizontally in the direction across the treatment tank 1 near the mean water level (MWL) above the low water level (LWL), and has a scum discharge port 3a that opens at the mean water level above the low water level. are doing. In addition, the above skimmer 3 is a low water level (LWL)
mean water level (MWL) between and high water level (HWL)
It can be installed anywhere as long as it is nearby. The skimmer 3 includes, as shown in FIG.
A scum discharge valve 9 is connected which is opened only at a predetermined time after the discharge process is completed. The aeration device 4 generates a circulating flow in the direction of the arrow (reflux direction) in the treatment tank 1 by spouting only liquid, and performs aeration by jetting out a gas-liquid mixture during the aeration process, and is a circulation pump. 10 and
It is composed of an aeration blower 11 which is controlled by switching, and achieves a sufficient stirring and mixing effect with a small amount of power by ejecting the gas-liquid mixture, that is, by shearing the jet flow and entraining the surrounding flow. Here, in the aeration step, both the circulation pump 10 and the aeration blower 11 are operated to blow out the gas-liquid mixture. However, since gas-liquid mixing is not required when the scum is advected in the direction of the skimmer 3 during a predetermined period of time after the discharge process is completed, only the circulation pump 10 is operated to generate only the circulation flow in the direction of the arrow. Even if you set this predetermined time with a timer,
It may also be set using the water level in the tank. Next, the operation of this invention will be explained. Inside the treatment tank 1, there is an aeration process in which the inflowing wastewater is aerated while generating a circulating flow in the direction of the arrow by ejecting the gas-liquid mixture from the aeration device 4, and the other process is to aerate the inflowing wastewater by stopping the air blowing and removing the liquid from the liquid. The operation of 1 cycle consisting of the precipitation step of precipitating the activated sludge and the discharge step of lowering the supernatant liquid discharge means 2 and discharging the supernatant liquid is repeated, and the activated sludge is continuously or optionally supplied from the inlet 1a. The inflowing sewage is mixed with activated sludge and treated. Further, the sludge in the treatment tank 1 is extracted at an appropriate time. Here, when the discharge process is completed, the liquid level is low and new sewage flows in from the inlet 1a. At almost the same time, only the circulation pump 10 of the aeration device 4 is activated, and only the liquid is ejected to generate a circulation flow, and by this circulation flow,
The scum is advected in the direction of the arrow in FIG. 1 and collected near the scum discharge port 3a of the skimmer 3 as shown in FIG. The water level in the treatment tank 1 gradually rises due to the inflowing wastewater, and when the liquid level in the tank reaches around the average water level above the low water level, a control device (not shown) is activated. Thus, the controlled scum discharge valve 9 changes from the closed state to the open state, and the scum is discharged to the outside of the treatment tank 1 together with the inflowing sewage. In this case, until the liquid level reaches around the average water level,
The scum is circulated within the treatment tank 1 by a circulation flow caused by only the liquid ejected from the aeration device 4. Therefore, by checking the time it takes for the water level to reach the vicinity of the average water level from a low water level and delaying it by setting a timer, it is possible to reduce the time during which the scum circulates within the processing tank 1. After a predetermined period of time (for example, about 3 to 5 minutes) has elapsed, the scum discharge valve 9 is closed, scum discharge is completed, and a new aeration process is started. The scum discharge valve 9 may be opened by a signal when the supernatant liquid discharge means 2 reaches a low water level and the downward movement of the supernatant liquid discharge means 2 is stopped. In this way, detection near the average water level is not necessary. Further, the scum may not be discharged every time, but may be discharged as needed.
以上のように、この発明によれば、放流工程終
了後に曝気装置の液噴出により、処理槽内で液循
環流を生起させることによつて、この液循環流で
スカムをスキマーに向け移送させ該スキマーから
円滑に排出させることができ、このため、水位が
変動する回分式活性汚泥処理槽のスカム排除を効
果的に確実に行うことができるという優れた効果
がある。
As described above, according to the present invention, by generating a liquid circulation flow in the treatment tank by liquid jetting from the aeration device after the discharge process is completed, the scum is transferred toward the skimmer by this liquid circulation flow. The scum can be smoothly discharged from the skimmer, which has the excellent effect of effectively and reliably removing scum from a batch type activated sludge treatment tank where the water level fluctuates.
第1図はこの発明の一実施例の平面図、第2図
は同縦断面図を示す。
1……回分式活性汚泥処理槽、2……上澄液排
出手段、3……スキマー、4……曝気装置。
FIG. 1 is a plan view of an embodiment of the present invention, and FIG. 2 is a longitudinal sectional view thereof. 1... Batch type activated sludge treatment tank, 2... Supernatant liquid discharge means, 3... Skimmer, 4... Aeration device.
Claims (1)
回分式活性汚泥処理槽と、この処理槽内に上下動
自在に配置され、上記放流工程時に上澄液を排出
する上澄液排出手段と、上記処理槽内の低水位よ
り上方の平均水位付近に設置され、上記放流工程
終了後、所定時間にわたつて開口されるスカム排
出用のスキマーと、上記処理槽内に配置され、曝
気工程時に気液混合液の噴出による曝気を行うと
共に、上記放流工程終了後の所定時間にわたつて
液のみの噴出により上記処理槽内に水平還流方向
への循環流を生起させることによつて槽内液中の
スカムを上記スキマーに向けて移流させる曝気装
置とを備えた汚水処理装置。1. A batch-type activated sludge treatment tank that repeats an aeration process, a precipitation process, and a discharge process, a supernatant liquid discharge means that is arranged vertically movably within this treatment tank and discharges a supernatant liquid during the above-mentioned discharge process, and the above-mentioned treatment A skimmer is installed near the average water level above the low water level in the tank and is opened for a predetermined period of time after the discharge process, and a skimmer is placed in the treatment tank to mix gas and liquid during the aeration process. In addition to aeration by jetting out the liquid, the scum in the liquid in the tank is removed by ejecting only the liquid over a predetermined period of time after the completion of the discharge process to generate a circulating flow in the horizontal reflux direction within the treatment tank. and an aeration device that advects water toward the skimmer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59129009A JPS618198A (en) | 1984-06-22 | 1984-06-22 | Sewage treatment apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59129009A JPS618198A (en) | 1984-06-22 | 1984-06-22 | Sewage treatment apparatus |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS618198A JPS618198A (en) | 1986-01-14 |
| JPS6350077B2 true JPS6350077B2 (en) | 1988-10-06 |
Family
ID=14998903
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP59129009A Granted JPS618198A (en) | 1984-06-22 | 1984-06-22 | Sewage treatment apparatus |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS618198A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6330547Y2 (en) * | 1984-10-23 | 1988-08-16 | ||
| US5286946A (en) * | 1992-09-02 | 1994-02-15 | Beloit Technologies, Inc. | Method and apparatus for securing an end of a headbox flow tube |
-
1984
- 1984-06-22 JP JP59129009A patent/JPS618198A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS618198A (en) | 1986-01-14 |
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