JPS60175598A - Sewage treatment method - Google Patents
Sewage treatment methodInfo
- Publication number
- JPS60175598A JPS60175598A JP59029641A JP2964184A JPS60175598A JP S60175598 A JPS60175598 A JP S60175598A JP 59029641 A JP59029641 A JP 59029641A JP 2964184 A JP2964184 A JP 2964184A JP S60175598 A JPS60175598 A JP S60175598A
- Authority
- JP
- Japan
- Prior art keywords
- treatment
- tanks
- sewage
- tank
- precipitation
- 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包・沈殿・放流の各工程
を繰返すことによシ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方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention is applied to batch activated sludge treatment in which wastewater is treated by repeating the steps of exposure, precipitation, and discharge in a treatment tank during normal operation. The present invention relates to a wastewater treatment method that can effectively treat wastewater even when the wastewater exceeds the above limit.
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単
一の処理槽内で、曝気Φ沈殿・放流の各工程を1サイク
ルとして処理を行うバッチ式活性汚泥処理法が注目され
ている。In activated sludge treatment, which has become mainstream in domestic wastewater treatment in recent years, the process of aeration, precipitation, and discharge is treated as one cycle in a single treatment tank that receives wastewater continuously or at any time. The batch-type activated sludge treatment method is attracting attention.
この処理法は沈殿槽および汚泥返送設備が不要である等
種々の利点があシ、極めて有効な処理法であるが、流入
汚水が設定値をはるかに越え友量である場合には、汚水
をそのまま流入するとオーバーフローしてしまうという
事態が生じる。This treatment method has various advantages such as not requiring a settling tank or sludge return equipment, and is an extremely effective treatment method. However, if the amount of inflowing sewage far exceeds the set value, If the water flows in as it is, an overflow situation will occur.
この発明は上記欠点を解消し、汚水流入量が設定値を越
えて流入してもそれに対応して処理、工程を変更し確実
な汚水処理が行える汚水処理方法を提供することを目的
とする。SUMMARY OF THE INVENTION An object of the present invention is to provide a sewage treatment method that eliminates the above-mentioned drawbacks and allows reliable sewage treatment by changing the treatment and process accordingly even if the amount of sewage inflow exceeds a set value.
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.
第1図はこの発明の方法が適用される処理装置の一例を
示し、複数(この実施例では2槽)設けられた処理槽1
,2と、この処理槽1,2に汚水を供給する汚水供給路
3と、処理槽1,2に沈殿した汚泥を引抜く汚泥引抜路
4と、汚泥を返送する返送路5とを有する。FIG. 1 shows an example of a processing apparatus to which the method of the present invention is applied.
, 2, a sewage supply path 3 for supplying sewage to the treatment tanks 1 and 2, a sludge extraction path 4 for pulling out the sludge settled in the treatment tanks 1 and 2, and a return path 5 for returning the sludge.
そして、各路3,4.5は第1および第2の処理槽1.
2の機能を交換できるように両槽1,2へそれぞれ接続
されている。Each passage 3,4.5 is connected to a first and a second treatment tank 1.
Both tanks 1 and 2 are connected to each other so that the functions of the two tanks can be exchanged.
また、上記処理槽1,2間は槽上部の越流口6で連通さ
れ、また、第2図、第3図(ここでは両槽とも同じ<m
造なのでその一方のみを示す。)に示すように、処理槽
1,2の底部には、曝気工程で汚水に曝気ブロア(図示
せず)、からの空気を吹込むための散気装置7が設けら
れている。そして槽上部には通常時、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8と、必要に
応じて固定堰9とが配置されている。In addition, the treatment tanks 1 and 2 are communicated with each other through an overflow port 6 at the top of the tank.
Since it is a construction, only one side is shown. ), an aeration device 7 is provided at the bottom of the treatment tanks 1 and 2 for blowing air from an aeration blower (not shown) into the wastewater during the aeration process. At the top of the tank, an automatic decanter 8 for discharging the supernatant liquid during the discharge process following the precipitation process, and a fixed weir 9 as necessary are arranged.
上記自動デカンタ8は回転可能な軸バイブ10に連結さ
れた排出パイプ11と、この排出パイプ11の自由端に
城付けられ、溢流口12aが開口された溢流管12と、
スカムバッフルを兼ねたフロート13とで構成されてい
る。そして、溢流管12が水面部にある状態では、処理
槽1,2内の上澄水は溢流口12aよシ溢流管12内に
流入し、軸パイプ10を経て外部へ放流される。また図
示しない回動手段によって溢流管12が液面よシ高い位
置になるように回動された状態では、処理槽1.2内の
液体の排水は行われない。The automatic decanter 8 includes a discharge pipe 11 connected to a rotatable shaft vibrator 10, an overflow pipe 12 attached to the free end of the discharge pipe 11, and having an overflow port 12a opened.
It is composed of a float 13 that also serves as a scum baffle. When the overflow pipe 12 is at the water surface, the supernatant water in the treatment tanks 1 and 2 flows into the overflow pipe 12 through the overflow port 12a, and is discharged to the outside through the shaft pipe 10. Further, when the overflow pipe 12 is rotated by a rotating means (not shown) so as to be at a position higher than the liquid level, the liquid in the processing tank 1.2 is not drained.
同、固定堰9からの排出は必要に応じてオン・オフされ
る。Similarly, the discharge from the fixed weir 9 is turned on and off as necessary.
次に、この発明の動作、作用について説明する。Next, the operation and effect of this invention will be explained.
通常時には、汚水を第1の処理槽1、第2の処理槽2に
順次切シ換えて流入し、各種1,2では散気装置7によ
る曝気、静置による沈殿、デカンタ8による放流を第4
図に示すように、順次切換え、通常のバッチ式活性汚泥
処理を行う。この際、例えば、第1の処理槽1で曝気工
程を、第2の処理槽2で沈殿、放流工程を行っていると
すると、汚水供給路3中の弁MA1 を閉弁MB、を開
とし、曝気工程中の処理槽へ汚水が流入されるように々
っている。Under normal conditions, sewage is switched to the first treatment tank 1 and second treatment tank 2 sequentially and flows into the first treatment tank 1 and second treatment tank 2, and in each type 1 and 2, aeration by the aeration device 7, sedimentation by standing still, and discharge by the decanter 8 are performed. 4
As shown in the figure, normal batch activated sludge treatment is performed by switching sequentially. At this time, for example, if the first treatment tank 1 is performing the aeration process and the second treatment tank 2 is performing the sedimentation and discharge process, the valve MA1 in the wastewater supply path 3 is closed and the valve MB is opened. , so that wastewater flows into the treatment tank during the aeration process.
次に緊急時、例えば、雨天時に汚水流入量が設定値以上
になった場合、汚水供給路3中の流量計14からの緊急
流量信号が発せられるが、汚水は引@続き開放されてい
る弁MB1を介して第1の処理槽lへ流入する。そして
、この緊急流量信号によって、第2の処理槽2内のデカ
ンタ8は連続放流のだめの所定の位置まで回動上昇する
。Next, in an emergency, for example, when the inflow of sewage exceeds a set value during rainy weather, an emergency flow signal is issued from the flow meter 14 in the sewage supply channel 3, but the sewage continues to flow through the open valve. It flows into the first processing tank l via MB1. Then, in response to this emergency flow rate signal, the decanter 8 in the second processing tank 2 is rotated and raised to a predetermined position of the continuous discharge reservoir.
この場合、汚水は第lの処理槽lで曝気処理を受けた後
、曝気混合液としてオーバーフロー(=よ)、第2の処
理槽2へ流入する。そして、第2の処理槽2で沈殿処理
され、水位が連続放流のための所定位置まで達すると、
沈殿上澄液がデカンタ8の溢流口12aおよび固定堰9
からオーバーフローして放流される。ここで、第2の処
理槽2内で沈殿した活性汚泥は返送路5中の弁MB3、
第2のポンプP2、弁MB□を介して第1の処理槽1へ
返送される。(返送路5中の弁MA3、第1のポンプP
1、弁MA2は当然、停止および閉状態である。)また
、第2の処理槽2内の余剰汚泥はポンプP3を介して汚
泥引抜路4によって適宜引抜かれる。In this case, the wastewater undergoes aeration treatment in the first treatment tank 1, and then overflows (=yo) as an aeration mixture and flows into the second treatment tank 2. Then, the water is subjected to sedimentation treatment in the second treatment tank 2, and when the water level reaches a predetermined position for continuous discharge,
The precipitated supernatant liquid flows through the overflow port 12a of the decanter 8 and the fixed weir 9.
It overflows and is discharged. Here, the activated sludge precipitated in the second treatment tank 2 is removed from the valve MB3 in the return path 5.
It is returned to the first processing tank 1 via the second pump P2 and valve MB□. (Valve MA3 in return path 5, first pump P
1. Valve MA2 is naturally stopped and closed. ) Also, excess sludge in the second treatment tank 2 is appropriately drawn out by the sludge drawing passage 4 via the pump P3.
このように、汚水は珂÷1の処理槽1で連続流入、連続
曝気後、第2の処理槽2へ自然流下し沈殿処理される。In this way, sewage continuously flows into the treatment tank 1 of 1/1, and after continuous aeration, flows naturally to the second treatment tank 2 where it is subjected to sedimentation treatment.
なお、この一連の処理があまシ長時間連続すると、第2
の処理槽2内の沈殿汚泥が部分的に滞留し、嫌気状態と
なり、効果的処理が行えなくなる。そこで、両処理槽1
.2の運転工程をタイマー等で逆にし、第2の処理41
12で曝気工程を、第lの処理槽1で沈殿・放流工程を
行うよう切シ換えると良い。この場合、曝気工程にあっ
た処理槽の沈殿が行われ、上澄放流が可能になるまで、
沈殿工程にあった処理槽を引き続き、沈殿工程に保持し
、ここに汚水を流入するようにする。Note that if this series of processing continues for a long time, the second
The precipitated sludge in the treatment tank 2 partially stagnates and becomes anaerobic, making it impossible to perform effective treatment. Therefore, both treatment tanks 1
.. 2 operation process is reversed using a timer etc., and the second process 41
It is preferable to switch the aeration process in step 12 so that the precipitation/discharge process is performed in the first treatment tank 1. In this case, sedimentation of the treatment tank that was in the aeration process is carried out until the supernatant can be discharged.
The treatment tank that was in the sedimentation process is kept in the sedimentation process, and wastewater is allowed to flow into it.
このとき、第5図に示すようにバックル15を設けると
、汚水の短絡放流が防止できる。また、処理槽1,2に
設けられた固定堰9は連続曝気工程時には水没している
。そこで、処理槽1.2の運転工程を逆にし、沈殿工程
を担当し、沈殿上澄液を排出する時においては、排出開
始後の一定量の処理水は汚水が流入されている処理槽(
つまJ7@気工程を担当する処理槽)へ返送される。な
お、上述のように固定堰9は通常時には、排出管のパル
プが閉じられ、排水が行なわれないようになっている。At this time, if a buckle 15 is provided as shown in FIG. 5, short-circuit discharge of waste water can be prevented. Further, the fixed weirs 9 provided in the treatment tanks 1 and 2 are submerged during the continuous aeration process. Therefore, the operating process of treatment tank 1.2 is reversed, and when it takes charge of the sedimentation process and discharges the sedimentation supernatant liquid, a certain amount of treated water after the start of discharge is transferred to the treatment tank into which the wastewater is flowing (
It is returned to Tsuma J7 (processing tank in charge of the air process). As mentioned above, in the fixed weir 9, the pulp of the discharge pipe is normally closed to prevent drainage.
さらに、連続放流は自動デカンタまたは固定堰9のみで
行ってもよい。Furthermore, continuous discharge may be performed only by an automatic decanter or fixed weir 9.
また、処理槽の担当交換の際画処理槽1.2の構造は同
じに形成され、汚泥供給路3、返送路5、汚泥引抜路4
が各々画処理槽1,2に対称接続されているので、ポン
プPl、P2 、P3 、弁MA1〜MA3、MB1〜
MB、を上述と逆の操作を行えばよい。In addition, when replacing the treatment tank, the structure of the treatment tank 1.2 is the same, sludge supply path 3, return path 5, sludge withdrawal path 4.
are symmetrically connected to the image processing tanks 1 and 2, respectively, so that the pumps Pl, P2, P3, valves MA1-MA3, MB1-
MB, by performing the operation opposite to that described above.
第5図は処理槽1.2の他の実施例(ここでもいずれか
一方の槽のみを示した。)を示し、上述の第1の実施例
と同様の処理を行うが、この実施例では、バッフル14
を設置し、プレリアクター16を区切っているので、流
入汚水が短絡放流されることがなく、また汚泥のバルキ
ングを防止できる。また連続処理時の曝気混合液を沈殿
処理を行っている処理槽のプレリアクター16へ流入で
きるようにすると沈殿効果がよい。さらに、処理槽1,
2に設けられた固定堰9は、上述の第1の実施例と同様
に通常時には排出管のパルプが閉じられ、排出が行われ
ないようになっている。FIG. 5 shows another embodiment of the treatment tank 1.2 (again, only one of the tanks is shown), in which the same processing as in the first embodiment described above is carried out, but in this embodiment, , baffle 14
Since the prereactor 16 is partitioned, the inflowing sewage is not short-circuited and discharged, and bulking of sludge can be prevented. Further, if the aerated liquid mixture during continuous treatment is allowed to flow into the prereactor 16 of the treatment tank in which the precipitation treatment is performed, the precipitation effect is improved. Furthermore, processing tank 1,
Similarly to the first embodiment described above, the fixed weir 9 provided at 2 is such that the pulp of the discharge pipe is normally closed and no discharge is performed.
第6図は散気装置7としてジェットエアレータを用いた
もので、上述の各実施例に適用するとよい。ジェットエ
アレ、−夕では圧力水と空気とが混合噴射される。この
圧力水として同一の処理槽1゜2内液を用いるのが一般
的であるが、この実施例では特に異常時の汚泥返送にこ
れを用いるとよい。FIG. 6 uses a jet aerator as the air diffuser 7, and is preferably applied to each of the above-mentioned embodiments. Jet Airle - In the evening, a mixture of pressurized water and air is injected. Although it is common to use the same liquid inside the treatment tank 1.2 as this pressure water, in this embodiment, it is particularly preferable to use this for returning sludge in the event of an abnormality.
つまシ沈殿工程にある処理槽1,2内の沈殿汚泥を引抜
き、これを曝気工程にある処理槽1,2内・のジェット
エアレータに供給するように切換えると良い。It is preferable to draw out the settled sludge in the treatment tanks 1 and 2 which are in the settling process and to supply this to the jet aerators in the treatment tanks 1 and 2 which are in the aeration process.
なお、この発明では曝気工程、連続曝気工程は、脱室な
どを促進するために、断続的に曝気を行うものを含むも
のとする。In addition, in this invention, the aeration process and the continuous aeration process include a process in which aeration is performed intermittently in order to promote escaping the room.
以上のようにこの発明によれば、汚水流入量が設計値を
越えて流入しても、それに対応させて処理工程を変更し
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 the design value, the treatment process can be changed accordingly to ensure reliable sewage treatment.
第1図はこの発明が適用される装置の概略的縦断面図、
第2図は同処理槽の概略的平面図、第3図は同概略的縦
断面図、第4図は各工程の手順図、第5図は処理槽の他
の実施例の縦断面図、第6図は散気装置の縦断面図を示
す。
1.2・・・処理槽、7・・・散気装置、8・・・デカ
ンタ。
特許出願人 株式会社 西原環境衛生研究所代理人 弁
理士 1) 澤 博 昭
(外2名)
図面の171τ(1(内容に変更なし)第1図
第2図
第4図
目−374jz梳
幻−4矢1艦
第6図
手続補正書(方式)
%式%
1、事件の表示 特願昭59−29641号2、発明の
名称
汚水処理方法
3、補正をする者
5、補正命令の日付
6、補正の対象
(1)願 書
(2)明細書
(3)図 面
7、補正の内容
(2)明細書の浄書(内容に変更なし)(3)図面の浄
書(内容に変更なし)
以上FIG. 1 is a schematic longitudinal sectional view of an apparatus to which this invention is applied;
Fig. 2 is a schematic plan view of the processing tank, Fig. 3 is a schematic longitudinal cross-sectional view of the same, Fig. 4 is a procedural diagram of each step, Fig. 5 is a longitudinal cross-sectional view of another embodiment of the processing tank, FIG. 6 shows a longitudinal sectional view of the air diffuser. 1.2... treatment tank, 7... aeration device, 8... decanter. Patent Applicant Nishihara Environmental Health Research Institute Co., Ltd. Representative Patent Attorney 1) Hiroshi Sawa (2 others) Drawing 171τ (1 (no change in content) Figure 1 Figure 2 Figure 4 - 374j phantom) 4 Arrow 1 Ship Figure 6 Procedural Amendment (Method) % Formula % 1. Indication of the case Japanese Patent Application No. 59-29641 2. Name of the invention Sewage treatment method 3. Person making the amendment 5. Date of amendment order 6. Subject of amendment (1) Application (2) Specification (3) Drawing 7, content of amendment (2) Engraving of specification (no change in content) (3) Engraving of drawing (no change in content)
Claims (1)
理するバッチ式活性汚泥処理槽に適用される汚水処理方
法であって、上記処理槽を複数設け、汚水の流入量が一
定量以上となった場合、上記処理槽の少なくとも一楢を
連続曝気槽に、少なくとも一槽を連続沈殿槽とし、上記
汚水を上記連続曝気槽に流入させ曝気処理後、上記連続
沈殿槽へ流入させ、ここで沈殿処理し、上澄液を放流し
、他方、沈殿汚泥を上記連続曝気槽へ返送することを特
徴とする汚水処理方法。A sewage treatment method that is applied to batch-type activated sludge treatment tanks that normally process sewage by repeating the steps of aeration, precipitation, and discharge, in which multiple treatment tanks are installed, and the inflow of sewage exceeds a certain amount. In this case, at least one of the treatment tanks is made into a continuous aeration tank and at least one tank is made into a continuous settling tank, and the wastewater is allowed to flow into the continuous aeration tank and after the aeration treatment, flow into the continuous settling tank. A sewage treatment method characterized in that the sludge is subjected to precipitation treatment, the supernatant liquid is discharged, and the settled sludge is returned to the continuous aeration tank.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59029641A JPS60175598A (en) | 1984-02-21 | 1984-02-21 | Sewage treatment method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59029641A JPS60175598A (en) | 1984-02-21 | 1984-02-21 | Sewage treatment method |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS60175598A true JPS60175598A (en) | 1985-09-09 |
JPS6345636B2 JPS6345636B2 (en) | 1988-09-09 |
Family
ID=12281705
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP59029641A Granted JPS60175598A (en) | 1984-02-21 | 1984-02-21 | Sewage treatment method |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60175598A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006312567A (en) * | 2005-05-09 | 2006-11-16 | Stec Kk | Method and apparatus for cutting work such as glass plate |
WO2007108175A1 (en) * | 2006-03-23 | 2007-09-27 | Matsushita Electric Industrial Co., Ltd. | Waste liquid treating apparatus |
-
1984
- 1984-02-21 JP JP59029641A patent/JPS60175598A/en active Granted
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006312567A (en) * | 2005-05-09 | 2006-11-16 | Stec Kk | Method and apparatus for cutting work such as glass plate |
WO2007108175A1 (en) * | 2006-03-23 | 2007-09-27 | Matsushita Electric Industrial Co., Ltd. | Waste liquid treating apparatus |
Also Published As
Publication number | Publication date |
---|---|
JPS6345636B2 (en) | 1988-09-09 |
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