JPS60232292A - Sewage treatment appratus - Google Patents
Sewage treatment appratusInfo
- Publication number
- JPS60232292A JPS60232292A JP59087840A JP8784084A JPS60232292A JP S60232292 A JPS60232292 A JP S60232292A JP 59087840 A JP59087840 A JP 59087840A JP 8784084 A JP8784084 A JP 8784084A JP S60232292 A JPS60232292 A JP S60232292A
- Authority
- JP
- Japan
- Prior art keywords
- sewage
- tank
- treatment
- aeration
- discharge
- 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
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)
Abstract
Description
【発明の詳細な説明】
この発明は通常時、処理槽内で曝気・沈殿・放流の各工
程を繰返すことにより汚水を処理するバッチ式活性汚泥
処理に適用され、特に流入汚水が一定量を越えた場合で
も汚水処理を効果的に行える汚水処理装置に関する。[Detailed Description of the Invention] This invention is normally applied to batch-type activated sludge treatment in which wastewater is treated by repeating the steps of aeration, precipitation, and discharge in a treatment tank. The present invention relates to a sewage treatment device that can effectively treat sewage even when
近年、生活排水処理の主流を占めている活性汚泥処理法
の中で汚水を連続的もしくは任意の時期に受け入れる処
理槽内で、曝気・沈殿・放流の各工程を繰返して処理を
行うバッチ式活性汚泥処理装置が注目されている。Among the activated sludge treatment methods that have become mainstream in domestic wastewater treatment in recent years, batch-type activated sludge treatment involves repeating the steps of aeration, precipitation, and discharge in a treatment tank that receives sewage continuously or at any time. Sludge treatment equipment is attracting attention.
このバッチ式処理装置は、従来主に工場廃本のように操
業時間(例えば8時間)のみ廃水が流入する場合に用い
られていたが、最近、下水のように連続して排出される
汚水の処理にも適用されるようになってきた。そして、
このような場合、処理槽を複数とし、曝気処理が行われ
ている檜へ順次流入し、未処理の汚水がそのまま放流さ
れるのを防止している。Batch-type treatment equipment has traditionally been used mainly when wastewater flows in only during operating hours (e.g. 8 hours), such as when wastewater is discharged continuously, such as sewage. It is also being applied to processing. and,
In such cases, a plurality of treatment tanks are provided, and the untreated wastewater is prevented from being discharged as it is by sequentially flowing into the cypress where the aeration treatment is being performed.
しかし、下水の場合、合流式では当然のみならず、たと
え分流式であっても雨天時に雨水が流入するため、流入
水量はかなり大量のものとなる。However, in the case of sewage, not only in a combined system, but even in a separate system, rainwater flows in during rainy days, so the amount of inflow water is quite large.
そこで、雨天時の最大流入量に対応させて槽容量を決定
しておかないと、雨天時には流入水量が多すぎ、檜から
オーバーフローしてしまうこととなる。しかし、このよ
うに槽容量を定めると、槽容量が非常に大きくなってし
まい、非現実的なものとなってしまう。Therefore, unless the tank capacity is determined in accordance with the maximum amount of inflow during rainy weather, the amount of inflowing water will be too large during rainy weather and will overflow from the cypress. However, if the tank capacity is determined in this way, the tank capacity will become extremely large, making it unrealistic.
この発明は上記欠点を解消し、汚水流入量が設定値を越
えて流入しても、汚水を他の静止状態の槽へ流入させる
ことによって、確実な汚水処理の行える汚水処理装置を
提供することを目的とする。The present invention solves the above-mentioned drawbacks and provides a sewage treatment device that can reliably treat sewage by allowing the sewage to flow into another stationary tank even if the amount of sewage inflow exceeds a set value. With the goal.
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。An embodiment of the present invention will be described below with reference to the drawings.
この発明は、第1図、第2図に示すように、曝気・沈殿
・放流の各工程を所定時間毎に繰返す複数(この実施例
では2槽)設けられた処理4%#A。As shown in FIGS. 1 and 2, this invention is a 4% treatment #A that is provided with a plurality of (two tanks in this example) in which each step of aeration, precipitation, and discharge is repeated at predetermined time intervals.
B(以下A槽、B槽という)と、この各人およびB槽に
汚水を順次切り換えて流入させる汚水切換部1とを有す
る。B (hereinafter referred to as A tank and B tank), and a sewage switching unit 1 that sequentially switches and causes sewage to flow into each person and the B tank.
上記A槽、B槽は第3図(第3図(A)はA槽の各工程
手順図、第3図(B)はB槽の同手順図を示す)K示す
ように、いずれか一方が曝気工程の場合、他方は沈殿あ
るいは放流工程になるように、相互間で工程の位相がず
れて処理を行うように予め設定されている。そして、こ
の人権、B檜の内部ハ、バッフル2によって、プレリア
クタ部3と、メインリアクタ部4とに区分され、このA
槽、B検量は、 H,W、L、より上方の槽壁に開口さ
れた連通口(汚水切換部)1で連通されている。また、
第2図に示すように、A槽、B槽の底部には、曝気工程
に汚水に曝気ブロア(図示せず)からの空気を吹込むた
めの散気装置5が設けられている。The above tanks A and B are shown in Figure 3 (Figure 3 (A) shows each process procedure diagram of tank A, and Figure 3 (B) shows the same procedure diagram of tank B). When one is an aeration process, the other is a precipitation or discharge process, so it is preset that the processes are carried out out of phase with each other. The inside of the B cypress is divided into a prereactor section 3 and a main reactor section 4 by a baffle 2, and this A
The tank and B calibration are connected through a communication port (sewage switching section) 1 opened in the tank wall above H, W, and L. Also,
As shown in FIG. 2, an aeration device 5 is provided at the bottom of tanks A and B for blowing air from an aeration blower (not shown) into the wastewater during the aeration process.
そして槽上部には、沈殿工程に続く放流工程時に上澄液
を排出する自動デカンタ6が配置されている。この自動
デカンタ6は回転可能な軸パイプ7に連結された排出パ
イプ8と、この排出パイプ8の自由端に取付けられ、溢
流口9&が開口された溢流管9と、スカムバッフルを兼
ねたフロー目Oとで構成されている。そして、溢流管9
が水面部にある状態では、A槽、B槽内の上澄水は溢流
口9aより溢流管9内に流入し、軸パイプ7を経て外部
へ放流される。また回動手段11によって溢流管9が液
面より高い位置になるように回動された状態では、槽内
液体の排水は行われない。An automatic decanter 6 is disposed at the top of the tank to discharge the supernatant during the discharge process following the precipitation process. This automatic decanter 6 includes a discharge pipe 8 connected to a rotatable shaft pipe 7, an overflow pipe 9 attached to the free end of the discharge pipe 8 and having an overflow port 9, and a scum baffle. It is composed of flow number O. And overflow pipe 9
When the water is at the water surface, the supernatant water in tanks A and B flows into the overflow pipe 9 through the overflow port 9a, and is discharged to the outside through the shaft pipe 7. Furthermore, when the overflow pipe 9 is rotated by the rotation means 11 so as to be at a position higher than the liquid level, the liquid in the tank is not drained.
尚、A槽、B槽への汚水aの供給は、例えば。In addition, the supply of wastewater a to tank A and tank B is as follows, for example.
ポンプビット12およびポンプ13からなる汚水供給装
置14により行われる。This is carried out by a waste water supply device 14 consisting of a pump bit 12 and a pump 13.
次に、この発明の動作1作用について説明する。Next, operation 1 of the present invention will be explained.
処理すべき汚水aは汚水供給装置14によって、平常時
、曝気を行っている一方の槽AまたはBへ順次流入され
、各種AまたはBでは、散気装置7による曝気、静置に
よる沈殿、デカンタ6による放流を第3図に示すように
順次行い、通常のバラ式活性汚泥処理を行う。The sewage a to be treated is sequentially flowed by the sewage supply device 14 into one tank A or B which normally performs aeration, and in each type A or B, aeration is performed by the aeration device 7, sedimentation is performed by standing still, and a decanter is performed. 6 is sequentially discharged as shown in FIG. 3, and normal bulk activated sludge treatment is performed.
次に、異常時、例えば、雨天時に汚水流入量が設定値以
上になった場合、プレリアクタ部3槽壁のH,W、Lよ
り上方に開口された連通口1から他方の槽へ汚水が流入
する。例えば、A槽へ流入している時間の汚水流入量が
異常に多いと、水位が上昇し、連通口1の位置にまで至
り、A槽内の汚水はB槽へ流入する。ここで、B槽は上
述のように沈殿または放流工程(この実施例では放流工
程、第3図(B)参照)にあるので、A槽より流入した
汚水aはプレリアクタ部3より、沈殿した活性汚泥と接
触し、汚水中の汚濁物質は活性汚泥に吸着され、浄化さ
れた後、放流される。Next, in the event of an abnormality, for example, when the amount of sewage inflow exceeds the set value during rainy weather, sewage flows into the other tank from the communication port 1 opened above H, W, and L of the pre-reactor 3 tank walls. Inflow. For example, if the amount of sewage flowing into tank A is abnormally large, the water level rises and reaches the position of communication port 1, and the sewage in tank A flows into tank B. Here, since the B tank is in the sedimentation or discharge process (in this example, the discharge process, see FIG. 3 (B)) as described above, the wastewater a flowing from the A tank is precipitated from the prereactor part 3. Upon contact with the activated sludge, pollutants in the wastewater are adsorbed by the activated sludge, purified, and then discharged.
この際、プレリアクタ部3を通常、曝気、攪拌を行わな
いようにすれば(固形物の堆積を防ぐため間欠的に曝気
してもよい)、A檜の活性汚泥がB槽へ流出しないので
、次回以降の処理に問題がない。また、処理槽は、バッ
フル2によって、プレリアクタ部3とメインリアクタ部
4とに区切っであるので、未処理の汚水が短絡放流され
ることがない。At this time, if the prereactor section 3 is normally not aerated or stirred (aerating may be performed intermittently to prevent solid matter accumulation), the activated sludge from the A cypress will not flow into the B tank. , there will be no problem with subsequent processing. Further, since the treatment tank is divided into a pre-reactor section 3 and a main reactor section 4 by the baffle 2, untreated wastewater will not be discharged in a short circuit.
従って、この実施例によれば、雨水等の混入より大量の
汚水が流入しても、問題なく処理が行え、また処理水質
も悪化することが少ない。なお、雨水等はBOD等は低
いため、静止状態の処理槽における活性汚泥との接触お
よび沈殿処理によって十分な処理が行える。Therefore, according to this embodiment, even if a larger amount of sewage flows in than rainwater or the like, it can be treated without any problems, and the quality of the treated water is unlikely to deteriorate. In addition, since rainwater and the like have low BOD, etc., sufficient treatment can be performed by contact with activated sludge and sedimentation treatment in a stationary treatment tank.
第4図は汚水切換部としてポンプを用いた他の実施例を
示す。この実施例では、A槽の混合液をB槽のプレリア
クタ部3へ流入させる第1のポンプ15と、B槽の混合
液をA槽のプレリアクタ部8へ流入させる第2のポンプ
16とによって、汚水切換部が構成されている。FIG. 4 shows another embodiment using a pump as the wastewater switching section. In this embodiment, a first pump 15 causes the mixed liquid in tank A to flow into the prereactor section 3 of tank B, and a second pump 16 causes the mixed liquid in tank B to flow into the prereactor section 8 in tank A. The waste water switching section is configured by:
従って、例えば、λ槽への汚水流入時に、流入水量が所
定量以上になると、A槽内の曝気混合液は、第1のポン
プ15でB槽へ輸送され、Al1内の水位が一定値以上
に々らないようにする。他方、B槽へ流入した混合液は
、ここで上述のように処理され、上澄液が放流される。Therefore, for example, when wastewater flows into the λ tank, when the amount of inflow water exceeds a predetermined amount, the aerated liquid mixture in tank A is transported to tank B by the first pump 15, and the water level in Al1 exceeds a certain value. Try not to get too excited. On the other hand, the mixed liquid flowing into tank B is treated here as described above, and the supernatant liquid is discharged.
所定の時刻になると、今度はB槽が曝気工程と碌り、こ
こに汚水が流入され、通常の処理が行われる。ここで、
前回と同様にB槽への流入量が所定量以上となると、第
2のポンプ16によって、B槽からA槽への混合液の移
送が行われ、同様に処理される。At a predetermined time, tank B starts the aeration process, wastewater flows into tank B, and normal treatment takes place. here,
As in the previous case, when the amount flowing into tank B exceeds a predetermined amount, the second pump 16 transfers the mixed liquid from tank B to tank A, where it is processed in the same way.
この際、時には一方の檜のMLSSが他種に比べ著しく
低くなっている場合もある。このような場合に備え、両
槽のMLSSを計測し、その差が一定以上となった場合
(曝気開始時は、水位が必ずり、W、Lなので、この時
のMLSS値を比較すると良い)、ポンプ輸送により、
その差を解消する。In this case, sometimes the MLSS of one type of cypress is significantly lower than that of the other type. In preparation for such a case, measure the MLSS of both tanks, and if the difference is above a certain level (at the start of aeration, the water level is always W and L, so it is a good idea to compare the MLSS values at this time) , by pumping,
Eliminate that difference.
この場合、曝気混合液を輸送してもよいし、沈殿汚泥の
方を輸送してもよい。In this case, the aerated mixture may be transported, or the settled sludge may be transported.
従って、この実施例によれば、大量の汚水が流入しても
通常の活性汚泥処理が行える。Therefore, according to this embodiment, normal activated sludge treatment can be carried out even if a large amount of wastewater flows in.
尚、汚水切換部は上述のように一方の槽内液の他種への
流入による手段だけでなく、汚水供給装置14の切換え
によって、汚水自体の流入を切換えて行ってもよい。ま
た、上記実施例では処理槽が2檜の場合について説明し
たが、これに限定されることなく、3檜以上でもよく、
所定量以上の汚水を静止状態の檜へ流入させればよい。The sewage switching section is not limited to the above-mentioned means of inflowing one type of liquid in the tank to another, but may also switch the inflow of sewage itself by switching the sewage supply device 14. Further, in the above embodiment, the case where the treatment tank has two cypresses has been described, but the treatment tank is not limited to this, and may be three or more cypresses.
It is only necessary to allow a predetermined amount or more of wastewater to flow into the cypress in a stationary state.
以上のようにこの発明によれば、汚水流入量が所定値を
越えて流入しても、汚水を他の静止状態の檜へ流入させ
ることによって、確実な汚水処理が行える等の極めて優
れた効果を有する。As described above, according to the present invention, even if the amount of sewage inflow exceeds a predetermined value, the sewage can be reliably treated by flowing the sewage into other cypresses in a stationary state. has.
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、第3図(A)はA檜の各工程の手順図、第3図(
B)はB槽の同手順図、第4図は他の実施例の平面図を
示す。
A、B・・・処理槽、I、15.16・・・汚水切換部
。Fig. 1 is a plan view of an embodiment of the present invention, Fig. 2 is a vertical cross-sectional view of the same, Fig. 3 (A) is a procedural diagram of each process of A-cypress wood, Fig. 3 (
B) shows the same procedure diagram of tank B, and FIG. 4 shows a plan view of another embodiment. A, B...Treatment tank, I, 15.16...Sewage switching section.
Claims (1)
の処理槽と、この各処理槽に汚水を順次切り換えて流入
させる汚水切換部とを備え、上記処理槽の少なくとも一
槽を沈殿あるいは放流工程にあるようにし、他の該処理
槽への所定時間内の汚水流入が一定量以上となった場合
、上記汚水切り換え部を介して余分の該汚水を沈殿ある
いは放流工程にある処理槽へ導入することを特徴とする
汚水処理装置。It is equipped with two or more treatment tanks that repeat the steps of aeration, sedimentation, and discharge at predetermined intervals, and a wastewater switching section that sequentially switches and flows wastewater into each of the treatment tanks, and at least one of the treatment tanks is used for sedimentation or discharge. If the inflow of sewage into another treatment tank exceeds a certain amount within a predetermined period of time, the excess sewage is sedimented or transferred to the treatment tank in the discharge process via the sewage switching section. A sewage treatment device characterized by the introduction of the system.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59087840A JPS60232292A (en) | 1984-05-02 | 1984-05-02 | Sewage treatment appratus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59087840A JPS60232292A (en) | 1984-05-02 | 1984-05-02 | Sewage treatment appratus |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS60232292A true JPS60232292A (en) | 1985-11-18 |
JPH0141114B2 JPH0141114B2 (en) | 1989-09-04 |
Family
ID=13926106
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP59087840A Granted JPS60232292A (en) | 1984-05-02 | 1984-05-02 | Sewage treatment appratus |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60232292A (en) |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5929641A (en) * | 1982-08-13 | 1984-02-16 | Ube Ind Ltd | Preparation of benzoic acid phenyl ester |
-
1984
- 1984-05-02 JP JP59087840A patent/JPS60232292A/en active Granted
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5929641A (en) * | 1982-08-13 | 1984-02-16 | Ube Ind Ltd | Preparation of benzoic acid phenyl ester |
Also Published As
Publication number | Publication date |
---|---|
JPH0141114B2 (en) | 1989-09-04 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
LAPS | Cancellation because of no payment of annual fees |