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JPH0139838B2 - - Google Patents
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JPH0139838B2 - - Google Patents

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Publication number
JPH0139838B2
JPH0139838B2 JP59255649A JP25564984A JPH0139838B2 JP H0139838 B2 JPH0139838 B2 JP H0139838B2 JP 59255649 A JP59255649 A JP 59255649A JP 25564984 A JP25564984 A JP 25564984A JP H0139838 B2 JPH0139838 B2 JP H0139838B2
Authority
JP
Japan
Prior art keywords
treatment tank
sewage
tank
aeration
sludge
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
Application number
JP59255649A
Other languages
Japanese (ja)
Other versions
JPS61136495A (en
Inventor
Noboru Hayakawa
Tomio Suzuki
Eiichi Nonaka
Takashi Tamaru
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.)
NISHIHARA KANKYO EISEI KENKYUSHO KK
Original Assignee
NISHIHARA KANKYO EISEI KENKYUSHO KK
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 NISHIHARA KANKYO EISEI KENKYUSHO KK filed Critical NISHIHARA KANKYO EISEI KENKYUSHO KK
Priority to JP59255649A priority Critical patent/JPS61136495A/en
Publication of JPS61136495A publication Critical patent/JPS61136495A/en
Publication of JPH0139838B2 publication Critical patent/JPH0139838B2/ja
Granted 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

Landscapes

  • Activated Sludge Processes (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 この発明は複雑な機構の上澄液排出装置を要し
ないで、所定時に汚水を処理槽内に流入させるだ
けで上澄液の放流排出が行える回分式の汚水処理
方法を提供することを目的とする。
[Detailed Description of the Invention] [Field of Industrial Application] This invention does not require a complicated supernatant liquid discharge device, and the supernatant liquid can be discharged by simply allowing wastewater to flow into a treatment tank at a predetermined time. The purpose is to provide a batch-type wastewater treatment method that can be carried out.

〔従来の技術〕[Conventional technology]

従来から回分式活性汚泥処理装置においては、
槽内水位が変動するため、上澄液排出装置が複雑
になり、水位が低い状態で運転する時間もあるた
め、有効容積が小さいという欠点があつた。
Conventionally, in batch type activated sludge treatment equipment,
Since the water level in the tank fluctuates, the supernatant liquid discharge device becomes complicated, and there are times when the water level is low, so the effective volume is small.

〔発明の概要〕[Summary of the invention]

この発明は上記欠点を解消するためになされた
ものであつて、流入汚水の曝気・沈殿・放流の各
処理工程を繰り返す単一の処理槽内での上記放流
に際し、その処理槽内に新たな汚水を供給して該
槽内の水位を強制的に上昇させることにより、複
雑な上澄液排出装置を必要とせず、上記沈殿工程
後の上澄液を円滑に効率よく放流させることがで
き、もつて、汚水処理効率の向上および槽内の有
効利用が図れる回分式の汚水処理方法を提供する
ことを目的とする。
This invention was made in order to eliminate the above-mentioned drawbacks, and when discharging inflow wastewater into a single treatment tank that repeats each treatment process of aeration, precipitation, and discharge, new water is added to the treatment tank. By supplying sewage and forcibly raising the water level in the tank, the supernatant liquid after the precipitation step can be smoothly and efficiently discharged without the need for a complicated supernatant liquid discharge device, It is an object of the present invention to provide a batch-type sewage treatment method that can improve sewage treatment efficiency and effectively utilize the inside of the tank.

〔発明の実施例〕[Embodiments of the invention]

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図に示した処理槽1は第2図に示すよう
に、曝気・沈殿・流入放流の各工程を繰り返して
汚水処理を行う。この処理槽1は、その上部に越
流ぜき2が設けられている。他方、その底部に
は、曝気工程で汚水に空気を吹込むための散気装
置3と、汚泥引き抜き部4とが設けられている。
そしてこの汚泥引き抜き部4で引抜かれた汚泥
は、別途処分される。
As shown in FIG. 2, the treatment tank 1 shown in FIG. 1 performs wastewater treatment by repeating the steps of aeration, sedimentation, and inflow and discharge. This treatment tank 1 is provided with an overflow weir 2 at its upper part. On the other hand, an aeration device 3 for blowing air into wastewater in the aeration process and a sludge drawing section 4 are provided at the bottom.
The sludge extracted by the sludge extraction section 4 is disposed of separately.

上記散気装置3は、通常、オン・オフ制御され
る曝気ブロア(図示せず)に接続されるが、この
時、例えば、気液混合液を噴出するジエツト式散
気装置のように目詰りしにくいものを用いるのが
好ましい。尚、6は短絡防止用のバツフルであ
る。このバツフル6により流入汚水は沈殿活性汚
泥と必ず接触、吸着されるので、未処理のまま上
澄液と共に排出されることはない。
The aeration device 3 is normally connected to an aeration blower (not shown) that is controlled on and off. It is preferable to use one that is difficult to clean. In addition, 6 is a buttful for short circuit prevention. Since the inflowing sewage is always brought into contact with and adsorbed by the precipitated activated sludge by this baffle 6, it is not discharged untreated together with the supernatant liquid.

上記貯留槽5は、処理すべき汚水を一旦貯留す
るものであつて、この貯留槽1内には処理槽1内
に汚水を供給するためのポンプ(汚水供給手段)
7が設置されている。
The storage tank 5 temporarily stores wastewater to be treated, and a pump (sewage supply means) for supplying wastewater into the treatment tank 1 is provided in the storage tank 1.
7 is installed.

次に、この発明の動作について説明する。 Next, the operation of the present invention will be explained.

処理すべき汚水は、まず、貯留槽5へ流入し、
ここに貯留される。そして、第2図に示すよう
に、各工程が繰り返される処理槽1が流入・放流
工程に移行すると、ポンプ7を駆動し、貯留槽5
内の汚水を処理槽1へ供給する。この汚水の流入
によつて、処理槽1内の水位は、曝気水位
(WL1)から上昇し、処理上澄液は越流ぜき2か
ら越流放流される。そして、流入・放流工程が終
了すると、汚泥引き抜き部4からの余剰汚泥の系
外への引き抜きまたは、引き抜いた汚泥等の槽内
液の貯留槽5への返送によつて、処理槽1内の水
位を曝気水位(WL1)まで下降させ、曝気工程
中に汚泥が越流しないようにして、曝気工程へ移
行する。
The wastewater to be treated first flows into the storage tank 5,
It will be stored here. As shown in FIG. 2, when the treatment tank 1, in which each process is repeated, shifts to the inflow/discharge process, the pump 7 is driven, and the storage tank 5
The wastewater inside is supplied to the treatment tank 1. Due to the inflow of this wastewater, the water level in the treatment tank 1 rises from the aeration level (WL 1 ), and the treated supernatant liquid is discharged overflow from the overflow weir 2. Then, when the inflow/discharge process is completed, the surplus sludge from the sludge extraction section 4 is pulled out of the system, or the tank liquid such as the extracted sludge is returned to the storage tank 5, thereby reducing the amount of water in the treatment tank 1. The water level is lowered to the aeration level (WL 1 ) to prevent sludge from overflowing during the aeration process, and the process moves to the aeration process.

このように、槽内水位を下降させるのは、曝気
工程時に汚泥が越流しないようにするためなの
で、第3図のように越流ぜき2を連動可動式とし
てもよい。
The purpose of lowering the water level in the tank in this way is to prevent sludge from overflowing during the aeration process, so the overflow weir 2 may be of an interlocking movable type as shown in FIG.

即ち、第3図aの越流ぜき2では、放流位置
(放流時)の越流口2aを曝気時には回動させ水
面上に保持する。また、第3図bでは、曝気時に
越流ぜき2を上昇させて、曝気工程時に越流ぜき
を水面方向に保持し曝気により汚泥が越流しない
ようにしている。また、曝気工程時に汚泥が越流
するのは制限せず、放流当初の汚泥の混入し上澄
液を貯留槽等へ返送するようにしてもよい。
That is, in the overflow weir 2 of FIG. 3a, the overflow port 2a at the discharge position (during discharge) is rotated and held above the water surface during aeration. In addition, in FIG. 3b, the overflow weir 2 is raised during aeration, and the overflow weir is held in the direction of the water surface during the aeration process to prevent sludge from overflowing due to aeration. Moreover, the overflow of sludge during the aeration process is not restricted, and the supernatant liquid mixed with sludge at the time of discharge may be returned to a storage tank or the like.

以上のように、この発明では放流工程時に処理
槽1内へ汚水を流入し、槽内水位を上昇させて処
理上澄液を越流排出させるので、複雑な構造を有
するデカンタ等の上澄液排出装置を用いることな
く効果的処理が行える。また槽内水位をほぼ一定
にできるので、容量の有効利用が図れる。
As described above, in this invention, wastewater flows into the treatment tank 1 during the discharge process, the water level in the tank is raised, and the treated supernatant liquid is discharged overflow, so the supernatant liquid is discharged from a decanter or the like having a complicated structure. Effective treatment can be performed without using a discharge device. Moreover, since the water level in the tank can be kept almost constant, the capacity can be used effectively.

第4図は処理槽1をA槽とB槽の2槽で構成し
た実施例である。両槽共、第5図に示す構造を成
しているが、A槽は第6図aのように、B槽は第
6図bのように処理工程が両者でずらしてある。
FIG. 4 shows an embodiment in which the processing tank 1 is composed of two tanks, tank A and tank B. Both tanks have the structure shown in FIG. 5, but the processing steps in tank A are shifted as shown in FIG. 6a, and in tank B as shown in FIG. 6b.

このように、処理槽1を2槽にし、汚水を順次
供給すれば、貯留槽から汚水をほぼ連続的に排出
することになり、貯留槽5の容量を小さくでき
る。
In this way, if the treatment tank 1 is made into two tanks and sewage is sequentially supplied, the sewage will be discharged from the storage tank almost continuously, and the capacity of the storage tank 5 can be reduced.

なお、2槽以上にすれば汚水の完全に連続的な
供給も可能である。
In addition, if two or more tanks are used, completely continuous supply of wastewater is also possible.

第7図および第8図は、曝気水位の上方の側壁
1a、越流ぜき2内側の汚れを洗浄可能とすると
共に、汚水を汚泥帯10の下部に分割流入する他
の実施例を示す。
FIGS. 7 and 8 show another embodiment in which dirt on the side wall 1a above the aeration water level and inside the overflow weir 2 can be washed, and sewage is dividedly introduced into the lower part of the sludge zone 10.

この実施例では、曝気水位〔WL1)の上方位
置に側壁1a、越流ぜき2内側に向けて液体を噴
射する複数のノズル8が配置され、水位の上下に
よつて壁面に付着する汚れをおとすことができ
る。
In this embodiment, a plurality of nozzles 8 that inject liquid toward the inside of the side wall 1a and the overflow weir 2 are arranged above the aeration water level [WL 1 can be lowered.

さらに、この実施例では、第1図、第5図で示
されるバツフル6は配置されていないが汚泥帯1
0の内部に汚水供給管11を配置し、汚水を分割
流入するようになつている。従つて上述の効果に
加え汚水汚泥との接触が効率的に行えるので、短
絡放流されにくく、さらに汚水が静かに流入でき
るので、沈殿汚泥が巻き上がり、汚泥が放流され
るおそれがない。
Furthermore, in this embodiment, although the baffle 6 shown in FIGS. 1 and 5 is not arranged, the sludge zone 1
A wastewater supply pipe 11 is arranged inside the tank 0, and the wastewater is divided into parts. Therefore, in addition to the above-mentioned effects, since contact with sewage and sludge can be carried out efficiently, it is difficult to cause short-circuit discharge, and furthermore, since sewage can quietly flow in, there is no risk of the settled sludge being rolled up and sludge being discharged.

また、バツフル6を設ければ、流入時の乱れは
さらに抑えられる。
Moreover, if the baffle 6 is provided, disturbances at the time of inflow can be further suppressed.

〔発明の効果〕〔Effect of the invention〕

以上のように、この発明によれば、曝気・沈
殿・放流工程を繰り返す回分式活性汚泥処理サイ
クルの中で、放流工程時にのみ汚水供給手段を稼
動させて処理槽内に汚水を強制流入させるので、
この汚水の強制流入による上記処理槽内の水位上
昇によつて、上記沈殿工程後の槽内上澄液を越流
ぜきから円滑に越流放出させることができ、この
ため、上記放流工程では複雑な上澄液排出装置を
一切必要とせずに上記沈殿工程後の上澄液を効率
よく放流させることができる。
As described above, according to the present invention, in the batch activated sludge treatment cycle in which aeration, precipitation, and discharge steps are repeated, the sewage supply means is operated only during the discharge step to forcefully flow sewage into the treatment tank. ,
By raising the water level in the treatment tank due to the forced inflow of sewage, the supernatant liquid in the tank after the precipitation process can be smoothly discharged from the overflow weir, and therefore, in the discharge process, The supernatant liquid after the precipitation step can be efficiently discharged without requiring any complicated supernatant liquid discharge device.

しかも、放流工程後には、上記汚水供給手段の
稼動を停止し、且つ上記処理槽内の余剰汚泥の系
外への引き抜きまたは汚泥等の槽内液を貯留槽へ
返送することにより、槽内水位を越流ぜきよりも
低く、即ち曝気しても越流ぜきから放出されない
水位まで低くする。この状態で上記曝気・沈殿工
程に移行するので、特に上記曝気工程中に槽内汚
泥が上記越流ぜきから越流放出されるようなこと
がない。また、上記曝気・沈殿工程の何れにおい
ても上澄液が上記越流ぜきから濫りに越流放出さ
れることもないため、構成が頗る簡単でコストダ
ウンが図れるものでありながら、上記回分式活性
汚泥処理サイクルを円滑かつ確実に繰り返すこと
ができ、汚水処理効率の向上および槽内容量の有
効利用が図れると共に、既存の処理槽にも容易に
適用できるなど、幾多の優れた効果がある。
Moreover, after the discharge process, the water level in the tank can be adjusted by stopping the operation of the sewage supply means, and by withdrawing excess sludge in the treatment tank to the outside of the system or returning tank liquid such as sludge to the storage tank. Lower the water level than the overflow weir, that is, lower the water level so that it will not be released from the overflow weir even if aerated. Since the aeration/sedimentation step is carried out in this state, the sludge in the tank will not be discharged overflow from the overflow weir, especially during the aeration step. In addition, in any of the above aeration and precipitation steps, the supernatant liquid is not discharged from the overflow weir into the overflow, so although the structure is extremely simple and costs can be reduced, the above batch type The activated sludge treatment cycle can be repeated smoothly and reliably, the sewage treatment efficiency can be improved, the capacity inside the tank can be effectively utilized, and it can be easily applied to existing treatment tanks, among other excellent effects.

また、この発明の実施態様では、上記処理槽内
の汚水流入側において、下部に開口をもつたバツ
フルを配設したので、上記処理槽内への流入汚水
は、該槽内で上記バツフルにより仕切り形成され
た汚水流入部に沈殿した活性汚泥の酸化吸着を受
け、次いで上記バツフルの下部開口に導かれ、こ
こでも沈殿した活性汚泥の下層部に流入して酸化
吸着を受けることにより浄化される。このため、
上記流入汚水は槽内汚泥との接触が効果的に行
え、短絡放流されず、更に汚水が静かに流入する
ので、沈殿汚泥が巻き上がらず、清澄な上澄液の
みを放流排出できるという効果がある。
Further, in the embodiment of the present invention, a buttful having an opening at the bottom is provided on the sewage inflow side of the treatment tank, so that the wastewater flowing into the treatment tank is partitioned by the buttful inside the tank. The precipitated activated sludge is oxidized and adsorbed in the formed sewage inlet, and then led to the lower opening of the baffle, where it also flows into the lower layer of the precipitated activated sludge and is purified by oxidation and adsorption. For this reason,
The above-mentioned inflowing sewage can effectively contact the sludge in the tank and will not be short-circuited and the sewage will flow in quietly, so the effect is that the settled sludge will not roll up and only the clear supernatant liquid can be discharged. be.

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

第1図はこの発明の一実施例の縦断面図、第2
図は処理槽の処理工程図、第3図は越流ぜきの可
動説明図、第4図は他の実施例の平面図、第5図
は同縦断面図、第6図は処理槽の処理工程図、第
7図は他の実施例の平面図、第8図は同縦断面
図、第9図は第8図のX−X線断面図を示す。 1……処理槽、2……越流ぜき、5……貯留
槽、7……ポンプ、11……汚水供給量。
Fig. 1 is a longitudinal cross-sectional view of one embodiment of the present invention;
The figure is a treatment process diagram of the treatment tank, Figure 3 is an explanatory diagram of the movement of the overflow weir, Figure 4 is a plan view of another embodiment, Figure 5 is a longitudinal cross-sectional view of the same, and Figure 6 is a diagram of the treatment tank. 7 is a plan view of another embodiment, FIG. 8 is a longitudinal sectional view thereof, and FIG. 9 is a sectional view taken along the line X--X of FIG. 8. 1...Treatment tank, 2...Overflow weir, 5...Storage tank, 7...Pump, 11...Sewage supply amount.

Claims (1)

【特許請求の範囲】[Claims] 1 流入汚水の曝気工程、沈殿工程および放流工
程を繰り返すことによつて汚水処理を行なう回分
式活性汚泥処理槽と、この処理槽内の上部に設け
られた上澄液放流用の越流ぜきと、上記処理槽内
に汚水を間歇的に供給する汚水供給手段とを備え
た汚水処理装置によつて行なわれる汚水処理方法
であつて、上記沈殿工程の終了後に上記汚水供給
手段を稼動させて上記処理槽内に新たな汚水を供
給し、これによつて上記処理槽内の水位を強制的
に上昇させて、上記沈殿工程の終了後に上記処理
槽内に生じた上澄液を上記越流ぜきから系外に越
流排出させることにより上記放流工程を行ない、
上記汚水供給手段の稼動を停止させることにより
上記放流工程を終了させ、ついで上記処理槽内か
ら汚泥等の槽内液を引き抜くことにより上記処理
槽内の水位を上記越流ぜきの上端よりも低い位置
まで下降させ、この状態で上記曝気・沈殿工程に
移行することを特徴とする汚水処理方法。
1. A batch-type activated sludge treatment tank that treats sewage by repeating the aeration process, precipitation process, and discharge process of inflow sewage, and an overflow weir installed at the top of this treatment tank for discharging supernatant liquid. and a sewage supply means for intermittently supplying sewage into the treatment tank. New wastewater is supplied into the treatment tank, thereby forcibly raising the water level in the treatment tank, and the supernatant liquid generated in the treatment tank after the completion of the sedimentation process is overflowed. The above discharge process is carried out by overflowing the water out of the system through the weir,
The discharge process is terminated by stopping the operation of the sewage supply means, and then the water level in the treatment tank is raised to be lower than the upper end of the overflow weir by drawing out tank liquid such as sludge from the treatment tank. A sewage treatment method characterized by lowering the wastewater to a low position and moving to the aeration/sedimentation step in this state.
JP59255649A 1984-12-05 1984-12-05 Sewage treatment tank Granted JPS61136495A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59255649A JPS61136495A (en) 1984-12-05 1984-12-05 Sewage treatment tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59255649A JPS61136495A (en) 1984-12-05 1984-12-05 Sewage treatment tank

Publications (2)

Publication Number Publication Date
JPS61136495A JPS61136495A (en) 1986-06-24
JPH0139838B2 true JPH0139838B2 (en) 1989-08-23

Family

ID=17281681

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59255649A Granted JPS61136495A (en) 1984-12-05 1984-12-05 Sewage treatment tank

Country Status (1)

Country Link
JP (1) JPS61136495A (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100423813B1 (en) * 2001-06-13 2004-03-30 대명엔텍(주) Biological wastewater disposal plant
NL1021466C2 (en) * 2002-09-16 2004-03-18 Univ Delft Tech Method for treating waste water.
KR20020083978A (en) * 2002-09-28 2002-11-04 주식회사 퍼텍코리아 CPA(Continuity inflow Periodic Activated-sludge System)PROCESS
JP5366402B2 (en) * 2007-05-14 2013-12-11 三菱レイヨン株式会社 Water treatment method

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS52101162U (en) * 1976-01-28 1977-08-01

Also Published As

Publication number Publication date
JPS61136495A (en) 1986-06-24

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