JPH02265699A - Batch activated sludge treatment method and device for sewage - Google Patents
Batch activated sludge treatment method and device for sewageInfo
- Publication number
- JPH02265699A JPH02265699A JP1088262A JP8826289A JPH02265699A JP H02265699 A JPH02265699 A JP H02265699A JP 1088262 A JP1088262 A JP 1088262A JP 8826289 A JP8826289 A JP 8826289A JP H02265699 A JPH02265699 A JP H02265699A
- Authority
- JP
- Japan
- Prior art keywords
- tank
- sewage
- treatment
- 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.)
- Granted
Links
- 239000010802 sludge Substances 0.000 title claims description 94
- 238000011282 treatment Methods 0.000 title claims description 86
- 239000010865 sewage Substances 0.000 title claims description 76
- 238000000034 method Methods 0.000 title claims description 37
- 238000005273 aeration Methods 0.000 claims description 59
- 230000008719 thickening Effects 0.000 claims description 48
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 28
- 239000006228 supernatant Substances 0.000 claims description 18
- 239000002351 wastewater Substances 0.000 claims description 16
- 238000001556 precipitation Methods 0.000 claims description 15
- 238000004062 sedimentation Methods 0.000 claims description 15
- 230000002265 prevention Effects 0.000 claims description 8
- 238000005192 partition Methods 0.000 claims description 7
- 238000002156 mixing Methods 0.000 claims description 3
- 208000028659 discharge Diseases 0.000 description 4
- 230000000694 effects Effects 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 238000004065 wastewater treatment Methods 0.000 description 2
- 230000002776 aggregation Effects 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000003292 glue Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 238000001179 sorption measurement 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)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は汚水の処理方法及びその装置に係り、特に曝気
、沈殿、排水処理を順次繰り返して汚水を処理する汚水
の回分式活性汚泥処理方法及びその装置に関する。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a method and apparatus for treating sewage, and particularly to a batch activated sludge treatment method for sewage in which sewage is treated by sequentially repeating aeration, precipitation, and wastewater treatment. and its apparatus.
従来、工場等から排出される汚水を回分式で活性汚泥処
理する場合、汚水を同一槽内で曝気処理した後、沈殿処
理して沈殿汚泥と上澄水とに分離し、上澄水は排水装置
で排水される。この場合、沈殿工程や排水工程中に、新
たな汚水を流入すると上澄水が乱流状態になり、分離し
た上澄水と汚泥とが再び混合し、市だ、流入した汚水も
上澄水や汚泥と混合するという問題がある。従って、汚
水を曝気処理中に流入する必要があるので、汚水の流入
時間が限定される。Conventionally, when sewage discharged from factories, etc. is treated with activated sludge in a batch manner, the sewage is aerated in the same tank, then subjected to sedimentation treatment to separate settled sludge and supernatant water, and the supernatant water is sent to a drainage system. Drained. In this case, when new sewage flows into the sedimentation process or drainage process, the supernatant water becomes turbulent, and the separated supernatant water and sludge mix again. There is a problem of mixing. Therefore, since the wastewater needs to flow in during the aeration process, the time for the wastewater to flow is limited.
そこで、この問題を解決すべく特公昭:18−3823
3号公報で沈殿工程や排水工程中でも汚水の放出が可能
な汚水の処理方法が開示されている。この処理方法は、
処理槽内に仕切壁を設けて新たに流入ゾーンを形成し、
仕切壁の下端部に開口部を設けて流入ゾーンと処理槽と
を連通させた汚水処理装置を使用することを特徴として
いる。Therefore, in order to solve this problem, Tokuko Sho: 18-3823
Publication No. 3 discloses a wastewater treatment method that allows wastewater to be discharged even during the precipitation process and the drainage process. This processing method is
A partition wall is installed inside the treatment tank to form a new inflow zone,
It is characterized by using a sewage treatment device in which an opening is provided at the lower end of the partition wall to communicate the inflow zone and the treatment tank.
この汚水処理装置によれば、汚水は流入ゾーンに流入し
、流入ゾーン内の汚水は仕切壁の開口部を介して処理槽
内に流入するので、沈殿工程や排水工程でも処理槽内の
汚水に乱流が生じない。従って、流入した汚水は処理槽
内の汚水と短絡しないので、曝気、沈殿、排水のいずれ
の処理中でも、処理槽に汚水を連続的に流入させること
が出来る。According to this sewage treatment equipment, sewage flows into the inflow zone, and the sewage in the inflow zone flows into the treatment tank through the opening in the partition wall, so even during the sedimentation process and the drainage process, the sewage in the treatment tank flows into the inflow zone. No turbulence occurs. Therefore, the inflowing sewage does not short-circuit with the sewage in the treatment tank, so that the sewage can continuously flow into the treatment tank during any of the aeration, precipitation, and drainage treatments.
しかしながら、この方法では処理槽から引抜かれた余剰
汚泥は濃度が低く、再度濃縮しなければ後工程の脱水処
理に困難をきたす。この為、a糊槽を外部に設;すで、
引抜いた余剰汚泥を再濃縮してから脱水処理している。However, in this method, the excess sludge extracted from the treatment tank has a low concentration, and unless it is concentrated again, it will be difficult to perform dewatering treatment in the subsequent process. For this reason, a glue tank is installed outside;
Excess sludge is reconcentrated and then dehydrated.
尚、再濃縮時の上澄水ま原汚水側に戻される。In addition, the supernatant water from the reconcentration is returned to the raw wastewater side.
従って、濃度の高い濃縮汚泥を得る為にa槽暗、引抜き
ポンプ、及び配管等の設備を外部に設けるので設備が大
型化し、又、濃縮槽での沈殿処理を効率良く行い引抜い
た汚泥の全量を濃縮汚泥とする為には、必要最小限の余
剰引抜量大維持する必要があるので操作が大変であると
いう問題がある。Therefore, in order to obtain highly concentrated thickened sludge, equipment such as tank A, a drawing pump, and piping must be installed externally, which increases the size of the equipment.Also, the sedimentation process in the thickening tank is carried out efficiently, and the total amount of sludge drawn out is In order to turn sludge into thickened sludge, it is necessary to maintain a large amount of surplus extraction at the minimum necessary level, which poses a problem in that the operation is difficult.
本発明はこのような事情に鑑みてなされたもので、簡素
なa縮処理設備と簡単な設備の操作で、高濃度のawJ
汚泥を得ることが出来る汚水の回分式活性汚泥処理方法
及びその装置を提供することを目的とする。The present invention was made in view of these circumstances, and uses simple a-condensation treatment equipment and simple equipment operation to treat high-concentration awJ.
An object of the present invention is to provide a batch activated sludge treatment method for sewage that can yield sludge, and an apparatus therefor.
〔課題を解決する為の手段〕
本発明は前記目的を達成するために、プレエアレーショ
ンタンクへ連続的に流入する汚水に濃縮槽から活性汚泥
を投入して混合汚水とし、該混合汚水を曝気処理した後
、処理槽に乱流防止状態で流入させ、処理槽内で前記沢
合汚水を曝気処理した後、沈殿処理して汚泥と上澄水と
に分離し、分離された上澄水を処理槽から排水し、前記
処理工程を工程順に繰り返すと共に、曝気工程中の前記
混合汚水、又は沈殿工程若しくは沈殿後の分離された汚
泥を処理槽内から濃縮槽に活性汚泥として流入させ、濃
縮槽に流入した活性汚泥を沈殿させて濃縮槽から排出し
、沈殿しない活性汚泥を濃縮槽からオーバーフローさせ
てプレエアレーションタンクへ投入することを特徴とし
ている。[Means for Solving the Problems] In order to achieve the above-mentioned object, the present invention adds activated sludge from a thickening tank to sewage that continuously flows into a pre-aeration tank to form mixed sewage, and aerates the mixed sewage. After that, the Sawaai sewage is allowed to flow into the treatment tank in a state that prevents turbulence, and the Sawaai sewage is aerated in the treatment tank, and then subjected to sedimentation treatment to be separated into sludge and supernatant water, and the separated supernatant water is released from the treatment tank. The water was drained, and the treatment steps were repeated in the order of steps, and the mixed sewage during the aeration step, or the sludge separated during the precipitation step or after the precipitation, was flowed from the treatment tank into the thickening tank as activated sludge, and then flowing into the thickening tank. The system is characterized in that the activated sludge is precipitated and discharged from the thickening tank, and the activated sludge that does not settle is allowed to overflow from the thickening tank and is charged into the pre-aeration tank.
また、本発明は前記目的を達成するために、処理槽内の
汚水を曝気、沈殿処理して汚泥と上澄水とに分離し、上
澄水を排水処理する汚水の回分式活性汚泥処理装置に於
いて、曝気工程中の混合汚水、又は沈殿工程若しくは沈
殿後の分離された汚泥が処理槽内から流入する濃縮槽と
、濃縮槽からオーバーフローした活性汚泥と、新たに放
出された汚水とが流入するプレエアレーションタンクと
、曝気工程時の混合汚水、又は沈殿工程若しくは沈殿後
の分離された汚泥を処理槽から濃縮槽に流入し、濃縮槽
に沈殿した汚泥を排出し、濃縮槽からプレエアレーショ
ンタンクにオーバーフローシタ活性汚泥と、プレエアレ
ーションタンクに新りに流入した汚水とを混合して混合
汚水とし、混合汚水を曝気処理してプレエアレーション
タンクから処理槽に乱流防止状態に流入させる処理装置
と、を設けたことを特徴としている。Furthermore, in order to achieve the above object, the present invention provides a batch type activated sludge treatment apparatus for sewage in which sewage in a treatment tank is subjected to aeration and precipitation treatment to separate it into sludge and supernatant water, and the supernatant water is treated as waste water. There is a thickening tank into which mixed sewage during the aeration process or separated sludge from the sedimentation process or after sedimentation flows from inside the treatment tank, activated sludge overflowing from the thickening tank, and newly released sewage flow into the thickening tank. A pre-aeration tank, mixed sewage during the aeration process, or separated sludge from the sedimentation process or after precipitation flows from the treatment tank into the thickening tank, the precipitated sludge is discharged into the thickening tank, and from the thickening tank it flows into the pre-aeration tank. A treatment device that mixes the overflow activated sludge and sewage that has newly flowed into the pre-aeration tank to form mixed sewage, aerates the mixed sewage, and causes the mixed sewage to flow from the pre-aeration tank into the treatment tank in a state of preventing turbulence; It is characterized by having the following.
本発明によれば、汚水はプレエアレーションタンク(1
6)で濃縮槽(14)から流入した活性汚泥と混合して
混合汚水となり混合汚水は曝気処理されて、流入管(3
2)と乱流防止板(30)とを介して処理槽(12)内
に乱流を生じさせずに流入し、曝気、沈殿処理で沈殿汚
泥と上澄水とに分離され、分離された上澄水は排水装置
(36)で排水される。According to the invention, the waste water is stored in a pre-aeration tank (1
6), it mixes with the activated sludge that has flowed in from the thickening tank (14) to become mixed sewage.The mixed sewage is aerated and flows into the inflow pipe (3).
2) and the turbulence prevention plate (30) into the treatment tank (12) without causing turbulence, and is separated into precipitated sludge and supernatant water through aeration and precipitation treatment. Clear water is drained by a drainage device (36).
上記工程を順次繰り返すと共に、曝気工程時の混合汚水
、又は沈殿工程若しくは沈殿後の分離された汚泥は活性
汚泥として移送ポンプ(26)で処理槽(12)から濃
縮槽(14)に流入され、濃縮槽(14)に沈殿した汚
泥は排出管(44)を経て排出される。C沈殿しない活
性汚泥は濃縮槽(14)からプレエアレーションタンク
(16)ニオ−ハーフローし、新たにエアレーション
タンク(16)に流入した汚水と混合して混合汚水とな
る。混合汚水は曝気処理され流入管(32)、乱流防止
板(30)から処理槽(12)内に流入する。While repeating the above steps sequentially, the mixed sewage during the aeration process or the sludge separated during the precipitation process or after the precipitation is flowed as activated sludge from the treatment tank (12) to the thickening tank (14) by the transfer pump (26), The sludge settled in the thickening tank (14) is discharged through the discharge pipe (44). The activated sludge that does not precipitate flows from the thickening tank (14) to the pre-aeration tank (16) and mixes with the sewage that has newly flowed into the aeration tank (16) to form mixed sewage. The mixed wastewater is aerated and flows into the treatment tank (12) through the inflow pipe (32) and the turbulence prevention plate (30).
従って、曝気処理以外の沈殿又は排出処理中でも汚水を
プレエアレーションタンク(16)を介して処理槽(1
2)内に流入させることが出来る。Therefore, even during precipitation or discharge treatment other than aeration treatment, wastewater is passed through the treatment tank (16) through the pre-aeration tank (16).
2) It can flow into the interior.
また、処理f!! (12)から濃縮槽(14)に流入
させた全ての汚泥を沈殿させる必要がないので必要最小
限の引抜量を維持する必要がなく、簡単な操作セ濃線種
(14)から高濃度の濃縮汚泥を引抜くことによって、
処理槽(12)内の汚泥濃度を所望値に維持することが
出来る。Also, processing f! ! Since there is no need to settle all of the sludge that has flowed into the thickening tank (14) from (12), there is no need to maintain the minimum necessary amount of sludge to be drawn out, and it is easy to operate from the thickening line type (14) to the high concentration sludge. By pulling out the thickened sludge,
The sludge concentration in the treatment tank (12) can be maintained at a desired value.
更に、濃縮処理設備を処理槽(12)と一体形にするこ
とが出来るので設備をコンパクト化することが出来る。Furthermore, since the concentration treatment equipment can be integrated with the treatment tank (12), the equipment can be made more compact.
以下添付図面に従って本発明に係る汚水の回分式活性汚
泥処理方法及びその装置の好ましい実施例を詳説する。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Preferred embodiments of the batch activated sludge treatment method and apparatus for wastewater according to the present invention will be described in detail below with reference to the accompanying drawings.
第1図に示す汚水処理装置10は、主に、処理h12、
a縮tvi 4、プレエアレーションタンク16から構
成されている。The sewage treatment equipment 10 shown in FIG. 1 mainly includes treatment h12,
It consists of a tvi 4 and a pre-aeration tank 16.
処理槽12は、主に、底面12A、壁B17、壁部18
とから形成され、その底面12Aには撹拌機20.20
が載設されている。撹拌機20.20は供給管22を介
してブロワ24に接続されている。また、この底面12
Aには移送ポンプ26が設けられ、この移送ポンプ26
には移送管28が接続されている。移送管28の排出−
28Aは後述する濃縮槽14の上方に設けられている。The processing tank 12 mainly includes a bottom surface 12A, a wall B17, and a wall portion 18.
and a stirrer 20.20 on the bottom surface 12A.
is included. The stirrer 20.20 is connected to the blower 24 via the supply pipe 22. Also, this bottom surface 12
A is provided with a transfer pump 26, and this transfer pump 26
A transfer pipe 28 is connected to. Discharge of transfer pipe 28-
28A is provided above the concentration tank 14, which will be described later.
更に、処理槽12の側壁17には乱流防止板30が設け
られ、乱流防止板30には流入管32の下端部が固定さ
れている。流入管32の上端部は壁面17を介して、後
述するプレエアレーションタンク16の設定水位Aに開
口している。従って、処理槽12の底部は流入管32を
介してプレエアレーションタンク16の設定水位への位
置に連通されている。また、処理槽12の壁面18には
、処理槽12の外側に開口している排水管34が設けら
れている。排水管34には上澄水を排出するための排出
口36が設けられている。排出口36は排出工程中は水
位Bの下降と共に下降する。Further, a turbulence prevention plate 30 is provided on the side wall 17 of the processing tank 12, and a lower end portion of an inflow pipe 32 is fixed to the turbulence prevention plate 30. The upper end of the inflow pipe 32 opens through the wall surface 17 to a set water level A of a pre-aeration tank 16, which will be described later. Therefore, the bottom of the treatment tank 12 is communicated via the inlet pipe 32 to the pre-aeration tank 16 at the set water level. Furthermore, a drain pipe 34 that opens to the outside of the processing tank 12 is provided on the wall surface 18 of the processing tank 12 . The drain pipe 34 is provided with an outlet 36 for discharging supernatant water. The discharge port 36 descends as the water level B decreases during the discharge process.
濃縮槽14は、主に、壁部38と壁部40とから形成さ
れ、壁部40の高さは壁部38の高さより低く、また、
壁部40はプレエアレーションタンク16の設定水位へ
より高く形成されている。The concentration tank 14 is mainly formed of a wall 38 and a wall 40, the height of the wall 40 is lower than the height of the wall 38, and
The wall portion 40 is formed higher than the set water level of the pre-aeration tank 16.
従って、濃縮槽14に汚水が供給されて満たされると、
汚水は壁部40の上端からオーバーフローして後述する
プレエアレーションタンクに流入する。濃縮槽14の上
部にはバッフルプレート42が壁部38に沿って左方向
に設けられている。又、壁部38の下端部には排泥管4
4が設けられているので、濃縮槽14に沈殿した汚泥は
排泥管44を介して濃縮槽14外に排出される。Therefore, when the concentration tank 14 is supplied with wastewater and filled,
Sewage overflows from the upper end of the wall portion 40 and flows into a pre-aeration tank to be described later. A baffle plate 42 is provided in the upper part of the concentration tank 14 along the wall 38 to the left. Further, a mud drainage pipe 4 is provided at the lower end of the wall portion 38.
4, the sludge settled in the thickening tank 14 is discharged to the outside of the thickening tank 14 via the sludge drain pipe 44.
プレエアレーションタンク16は、主に、壁部40と壁
部17とか形成され、その底部には散気装置46が設け
られている。散気装置46は供給管22を介してブロワ
24に接続されている。このプレエアレーションタンク
16の上方には汚水放出管48の放出口48Aが設けら
れている。The pre-aeration tank 16 is mainly formed with a wall portion 40 and a wall portion 17, and an air diffuser 46 is provided at the bottom thereof. The air diffuser 46 is connected to the blower 24 via the supply pipe 22. A discharge port 48A of a sewage discharge pipe 48 is provided above the pre-aeration tank 16.
前記の如く構成された本発明に係る汚水の回分式活性汚
泥処理方法及びその装置の作用について説明する。The operation of the batch-type activated sludge treatment method for sewage and the apparatus configured as described above according to the present invention will be explained.
工場等から廃水された汚水は汚水放出管48を経て放出
口48Aからプレエアレーションタンク16内に流入す
る。プレエアレーションタンク16に流入した汚水は、
濃縮槽14からオーバーフローした活性汚泥と混合して
混合汚水となり、ブロア24、供給管22を介して散気
装置46から放出されている気泡で曝気処理される。Sewage discharged from factories and the like flows into the pre-aeration tank 16 through the sewage discharge pipe 48 and the discharge port 48A. The sewage that has flowed into the pre-aeration tank 16 is
It mixes with the activated sludge overflowing from the thickening tank 14 to become mixed sewage, which is aerated with air bubbles released from the air diffuser 46 via the blower 24 and supply pipe 22.
・曝気処理された混合汚水は設定水位Aを越すと流入管
32と乱流防止板30とを介して処理槽12の底部に流
入する。処理槽12に流入した混合汚水は処理槽12内
の活性汚泥と共に攪拌機20.20で混合、曝気処理さ
れて活性汚泥となり、その後の沈殿処理で、汚泥と上澄
水とに分離される。- When the aerated mixed wastewater exceeds the set water level A, it flows into the bottom of the treatment tank 12 via the inflow pipe 32 and the turbulence prevention plate 30. The mixed sewage that has flowed into the treatment tank 12 is mixed with the activated sludge in the treatment tank 12 by an agitator 20, 20, and is aerated to become activated sludge, which is then separated into sludge and supernatant water by a subsequent sedimentation process.
分離された上澄水は下降する排水口36、排水管34を
経て処理槽12の外側に排水される。The separated supernatant water is drained to the outside of the treatment tank 12 through a descending drain port 36 and a drain pipe 34.
上記工程を順次繰り返すと共に、曝気工程時の混合汚水
、又は沈殿工程若しくは沈殿後の分離された汚泥は処理
槽12内から移送ポンプ26で吸い上げられ、移送管2
8を経て活性汚泥として濃縮槽14に移送される。この
場合、活性汚泥は、壁部38とバラフールプレート42
との間に放出されるので、放出された活性汚泥はプレエ
アレーションタンク16にオーバーフローせずに濃縮槽
14内に一旦貯えられる。従って、貧線種14には汚泥
が沈殿し、沈殿した汚泥は排泥管44を経て濃縮槽14
から排出される。このように、濃縮槽14に沈殿する汚
泥は処理槽12の汚泥が再沈殿するので、処理槽12の
沈殿汚泥より密度が高くなる。又、濃縮槽14に排泥管
44が設けられているので、沈殿した汚泥をスムーズに
排出することが出来る。While repeating the above steps sequentially, the mixed sewage during the aeration process or the separated sludge during the precipitation process or after the precipitation is sucked up from the treatment tank 12 by the transfer pump 26, and the transfer pipe 2
8 and is transferred to a thickening tank 14 as activated sludge. In this case, the activated sludge is distributed between the wall portion 38 and the barafour plate 42.
Therefore, the released activated sludge is temporarily stored in the thickening tank 14 without overflowing into the pre-aeration tank 16. Therefore, sludge is precipitated in the poor grade 14, and the precipitated sludge passes through the sludge pipe 44 to the thickening tank 14.
is discharged from. In this way, the sludge that settles in the thickening tank 14 has a higher density than the precipitated sludge in the treatment tank 12 because the sludge in the treatment tank 12 is reprecipitated. Further, since the thickening tank 14 is provided with the sludge drain pipe 44, the settled sludge can be smoothly drained.
また、沈殿しない活性汚泥が濃縮槽14内に充満すると
、この活性汚泥は壁部40をオーバーフローしてプレエ
アレーションタンク16内に流入する。この場合、aw
i槽14に発生したスカムは汚水と共にプレエアレーシ
ョンタンクに流入するので、スカムは濃縮槽I4に滞留
しない。プレエアレーンフンタンク16内に流入した活
性汚泥は、汚水放出管48の放出口48Aから流入され
た汚水と共に、前記と同様に散気装置46で曝気処理さ
れ、初期吸着作用で沈降し易い汚水に生成されると共に
酸素の供給で腐敗の防止が可能になる。Furthermore, when the activated sludge that does not precipitate fills the thickening tank 14, this activated sludge overflows the wall portion 40 and flows into the pre-aeration tank 16. In this case, aw
Since the scum generated in the i-tank 14 flows into the pre-aeration tank together with the waste water, the scum does not stay in the concentration tank I4. The activated sludge that has flowed into the pre-air lane sump tank 16 is aerated with the sewage that has flowed in from the discharge port 48A of the sewage discharge pipe 48 in the same way as described above, and is treated by the aeration device 46 to eliminate sewage that tends to settle due to the initial adsorption action. It is possible to prevent spoilage by supplying oxygen.
従って、処理槽内の上澄水との短絡を防止することが出
来る。また・、プレエアレーションタンク16は、流入
管32、乱流防止板30を介して処理槽12に連通して
いるので、プレエアレーションタンク16から処理槽1
2内に活性汚泥を流入しても処理槽12の活性汚泥に乱
流が生じない。以下前記処理工程の順に各工程が繰り返
されて汚水が処理される。Therefore, short circuit with the supernatant water in the treatment tank can be prevented. Furthermore, since the pre-aeration tank 16 is connected to the processing tank 12 via the inflow pipe 32 and the turbulence prevention plate 30, the pre-aeration tank 16 communicates with the processing tank 12
Even when the activated sludge flows into the treatment tank 12, turbulence does not occur in the activated sludge in the treatment tank 12. Thereafter, each process is repeated in the order of the above treatment steps to treat the wastewater.
以上説明したように本発明に係る汚水の回分式活性汚泥
処理方法及びその装置によれば、プレエアレージョンタ
ンクで予め曝気処理した混合汚水を処理槽に乱流を生じ
させずに流入するので、汚水の処理能力を低下させずに
、曝気、沈殿、又は排出処理中でも処理槽に汚水を放出
することが出来る。As explained above, according to the batch-type activated sludge treatment method and apparatus for sewage according to the present invention, mixed sewage that has been aerated in advance in the pre-aeration tank can flow into the treatment tank without causing turbulence. The sewage can be discharged into the treatment tank even during aeration, sedimentation, or discharge treatment without reducing the sewage treatment capacity.
また、プレエアレーションタンクに新たに流入した汚水
は濃m槽から流入した活性汚泥と混合して混合汚水とな
り、混合汚水が曝気処理されて処理槽に流入するので、
処理槽内の底部にa縮汚泥が沈殿し易く、更に、濃縮槽
で処理槽内の底部に沈殿した濃縮汚泥が再沈殿するので
、高濃度の濃縮汚泥を濃縮槽から排出することが出来る
。In addition, the new sewage that has flowed into the pre-aeration tank mixes with the activated sludge that has flowed from the thickened tank to become mixed sewage, and the mixed sewage is aerated and flows into the treatment tank.
The a-shrinkage sludge easily settles at the bottom of the treatment tank, and the thickened sludge that has settled at the bottom of the treatment tank in the thickening tank is reprecipitated, so highly concentrated thickened sludge can be discharged from the thickening tank.
更に、濃縮槽からプレエアレーションタンクに活性汚泥
を流入するので、濃縮槽内に流入された汚泥全量を沈殿
させる必要がない。従って、模作が簡単なコンパクトな
設備で余剰汚泥のa縮性の向上を図ることが出来る。Furthermore, since the activated sludge flows from the thickening tank into the pre-aeration tank, there is no need to precipitate the entire amount of sludge that has flowed into the thickening tank. Therefore, it is possible to improve the aggregation properties of excess sludge using compact equipment that is easy to replicate.
第1図は本発明に係る汚水の回分式活性汚泥処理装置の
断面図である。
IO・・・汚水処理装置、 12川処理槽、 14・
・・amW、 16・・・プレエアレーションタンク
、26・・・移送ポンプ、 3o・・・乱流防止板、
32・・・流入管、 42・・・パフフルプレート、
44・・・排泥管、 48・・・汚水放出管、 A
、B・・・設定水位。FIG. 1 is a sectional view of a batch-type activated sludge treatment apparatus for wastewater according to the present invention. IO...sewage treatment equipment, 12 river treatment tank, 14.
... amW, 16... pre-aeration tank, 26... transfer pump, 3o... turbulence prevention plate,
32... Inflow pipe, 42... Puffful plate,
44...Sludge drainage pipe, 48...Sewage discharge pipe, A
, B... Set water level.
Claims (3)
水に濃縮槽から活性汚泥を投入して混合汚水とし、 該混合汚水を曝気処理した後、処理槽に乱流防止状態で
連続的に流入させ、 処理槽内で前記混合汚水を曝気処理した後、沈殿処理し
て汚泥と上澄水とに分離し、 分離された上澄水を処理槽から排水し、 前記処理工程を工程順に繰り返すと共に、処理槽におけ
る曝気工程中の前記混合汚水、又は沈殿工程若しくは沈
殿後の分離された汚泥を処理槽内から濃縮槽に活性汚泥
として流入させ、 濃縮槽に流入した活性汚泥を沈殿させて濃縮槽から排出
し、 沈殿しない活性汚泥を濃縮槽からオーバーフローさせて
プレエアレーションタンクへ投入することを特徴とした
汚水の回分式活性汚泥処理方法。(1) Activated sludge is added from the thickening tank to the sewage that continuously flows into the pre-aeration tank to form mixed sewage, and after the mixed sewage is aerated, it is continuously flowed into the treatment tank in a state that prevents turbulence. After the mixed sewage is aerated in the treatment tank, it is separated into sludge and supernatant water by sedimentation treatment, the separated supernatant water is drained from the treatment tank, and the above treatment steps are repeated in the order of the steps, and the water in the treatment tank is The mixed sewage during the aeration process, or the sludge separated during the precipitation process or after the precipitation, flows from the treatment tank into the thickening tank as activated sludge, and the activated sludge that has flowed into the thickening tank is precipitated and discharged from the thickening tank, A batch activated sludge treatment method for sewage characterized by overflowing unsettled activated sludge from a thickening tank and charging it into a pre-aeration tank.
水とに分離し、上澄水を排水処理する汚水の回分式活性
汚泥処理装置に於いて、 曝気工程中の混合汚水、又は沈殿工程若しくは沈殿後の
分離された汚泥が処理槽内から流入する濃縮槽と、 濃縮槽からオーバーフローした活性汚泥と、新たに放出
された汚水とが流入するプレエアレーションタンクと、 曝気工程時の混合汚水、又は沈殿工程若しくは沈殿後の
分離された汚泥を処理槽から濃縮槽に流入し、濃縮槽に
沈殿した汚泥を排出し、濃縮槽からプレエアレーション
タンクにオーバーフローした活性汚泥と、プレエアレー
ションタンクに新たに流入した汚水とを混合して混合汚
水とし、混合汚水を曝気処理してプレエアレーションタ
ンクから処理槽に乱流防止状態に流入させる処理装置と
、を設けたことを特徴とする汚水の回分式活性汚泥処理
装置。(2) In a sewage batch activated sludge treatment equipment that aerates and settles sewage in a treatment tank to separate it into sludge and supernatant water, and then treats the supernatant water as wastewater, mixed sewage during the aeration process, or A thickening tank into which sludge separated during the sedimentation process or after settling flows into the treatment tank; a pre-aeration tank into which activated sludge overflowing from the thickening tank and newly released sewage flow; and a mixing tank during the aeration process. Sewage or sludge separated from the sedimentation process or after settling flows into the thickening tank from the treatment tank, the settled sludge is discharged into the thickening tank, activated sludge overflows from the thickening tank into the pre-aeration tank, and activated sludge flows into the pre-aeration tank. A treatment device for mixing newly inflowing sewage to form mixed sewage, aerating the mixed sewage, and causing the mixed sewage to flow from a pre-aeration tank into a treatment tank in a state of preventing turbulence. type activated sludge treatment equipment.
水、又は沈殿工程若しくは沈殿後の分離された汚泥を活
性汚泥として濃縮槽に移送する移送装置と、 処理槽から移送された活性汚泥が濃縮槽に流入する時、
プレエアレーションタンクと短絡してオーバーフローし
ないように、濃縮槽に設けられたバッフルプレートと、 濃縮槽に設けられ、濃縮槽に沈殿した汚泥を排出する排
泥管と、 濃縮槽とプレエアレーションタンクとを仕切り、濃縮槽
とプレエアレーションタンクとの他の壁部より低く形成
された仕切壁と、 プレエアレーションタンクに設けられ、曝気処理を行う
散気装置と、 仕切壁より低く設定されたプレエアレーションタンクの
設定水位に開口して設けられ、プレエアレーションタン
クと処理槽とを連通した流入管と、流入管の排水口に設
けられ、排水口から汚水が流入した時、処理槽内の汚水
の乱流を防止する乱流防止板と、 を有することを特徴とする請求項(2)記載の汚水の回
分式活性汚泥処理装置。(3) The treatment device includes a transfer pump installed in the treatment tank to transfer the mixed sewage during the aeration process or the separated sludge after the sedimentation process or sedimentation to the thickening tank as activated sludge; When activated sludge transferred from the tank flows into the thickening tank,
In order to prevent overflow due to short circuit with the pre-aeration tank, a baffle plate installed in the thickening tank, a sludge pipe installed in the thickening tank to discharge the sludge settled in the thickening tank, and a thickening tank and pre-aeration tank are installed. Partition, a partition wall formed lower than other walls of the thickening tank and pre-aeration tank, an aeration device installed in the pre-aeration tank for aeration processing, and a partition wall set lower than the partition wall of the pre-aeration tank. It is installed at the inflow pipe that opens at a set water level and communicates the pre-aeration tank and the treatment tank, and at the drain port of the inflow pipe, and prevents the turbulent flow of sewage in the treatment tank when sewage flows in from the drain port. The batch activated sludge treatment apparatus for wastewater according to claim 2, further comprising: a turbulence prevention plate for preventing turbulence.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1088262A JP2712521B2 (en) | 1989-04-06 | 1989-04-06 | Batch activated sludge treatment method and apparatus for wastewater |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1088262A JP2712521B2 (en) | 1989-04-06 | 1989-04-06 | Batch activated sludge treatment method and apparatus for wastewater |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH02265699A true JPH02265699A (en) | 1990-10-30 |
| JP2712521B2 JP2712521B2 (en) | 1998-02-16 |
Family
ID=13937969
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1088262A Expired - Fee Related JP2712521B2 (en) | 1989-04-06 | 1989-04-06 | Batch activated sludge treatment method and apparatus for wastewater |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2712521B2 (en) |
-
1989
- 1989-04-06 JP JP1088262A patent/JP2712521B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JP2712521B2 (en) | 1998-02-16 |
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