JP2579295B2 - Wastewater treatment equipment - Google Patents
Wastewater treatment equipmentInfo
- Publication number
- JP2579295B2 JP2579295B2 JP25808988A JP25808988A JP2579295B2 JP 2579295 B2 JP2579295 B2 JP 2579295B2 JP 25808988 A JP25808988 A JP 25808988A JP 25808988 A JP25808988 A JP 25808988A JP 2579295 B2 JP2579295 B2 JP 2579295B2
- Authority
- JP
- Japan
- Prior art keywords
- biological treatment
- treatment tank
- baffle plate
- wastewater
- wastewater treatment
- 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 - Fee Related
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
- Biological Treatment Of Waste Water (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は,下廃水,汚濁した河川湖沼水等を処理する
廃水処理装置に関し,特に,微生物を付着させた粒状担
体と廃水と酸素含有気体とからなる三相流動層を生じさ
せ,廃水を生物処理して清澄水とする流動生物処理型の
廃水処理装置に関する。Description: TECHNICAL FIELD The present invention relates to a wastewater treatment apparatus for treating sewage, polluted river water, and the like, and more particularly, to a granular carrier to which microorganisms are attached, wastewater, and an oxygen-containing gas. The present invention relates to a fluidized biological treatment type wastewater treatment apparatus which generates a three-phase fluidized bed comprising:
生物処理槽内に流動化させた粒状担体の表面に微生物
を付着させ,流動層内に配設した散気装置を介して曝気
を行って水中の汚濁物質を除去する三相流動層法は,他
の生物膜法に比べて微生物の付着に供する担体の表面積
が飛躍的に大きくとれるため槽内に多量の微生物を保持
することが可能となり,その結果,高速,高負荷処理が
実現できるため,最近特に注目を集めている。しかし,
通気により乱された流動層中からの担体粒子の飛び出し
による処理水中への担体粒子の流出を如何に防止するか
が重要なポイントであった。The three-phase fluidized-bed method, in which microorganisms adhere to the surface of the granular carrier fluidized in the biological treatment tank and aeration is performed through an air diffuser arranged in the fluidized bed to remove pollutants in water, Compared to other biofilm methods, the surface area of the carrier used for the attachment of microorganisms can be dramatically increased, so that a large amount of microorganisms can be retained in the tank. As a result, high-speed, high-load processing can be realized. Recently, it has attracted particular attention. However,
An important point was how to prevent the carrier particles from flowing into the treated water due to the ejection of the carrier particles from the fluidized bed which was disturbed by the ventilation.
この流出を防止するものとして,特開昭61−268395号
公報には,流動床生物処理装置の槽内に液及び固体粒子
は通過し得るが,気泡は通過し得ない大きさの開口を多
数有する傾斜した隔壁を設けて担体粒子の処理水中への
流出を防止する技術が開示されている。空気気泡の大き
さは水中に酸素を効果的に溶解させるために小さい方が
好ましいことは当業界においては周知の事実である。し
かしながら,上記の方法では気泡の大きさを大きくせざ
るを得ないため,担体の流出は効果的に防止できるもの
の,肝心の廃水処理効果が低下するという欠点が生じ
る。To prevent this outflow, Japanese Patent Application Laid-Open No. 61-268395 discloses a large number of openings having a size that allows liquids and solid particles to pass through, but does not allow air bubbles to pass into the tank of a fluidized-bed biological treatment apparatus. There is disclosed a technology for preventing carrier particles from flowing into treated water by providing an inclined partition having the same. It is well known in the art that the size of the air bubbles is preferably small in order to effectively dissolve oxygen in water. However, in the above method, since the size of the air bubbles must be increased, the outflow of the carrier can be effectively prevented, but there is a disadvantage that the essential wastewater treatment effect is reduced.
このような廃水処理効果の低下を引き起こす気泡径の
増大を必要としないで担体粒子の流出を防止するものと
して,特開昭52−137154号公報には,気液接触反応槽の
上部が下部より大きな断面積を有するように形成し,該
反応槽の広くなった部分に下端の断面積が槽下部の断面
積より大きい気液分離筒壁を配置して担体粒子の処理水
中への流出防止を図った技術が開示されている。Japanese Patent Application Laid-Open No. 52-137154 discloses that the upper part of a gas-liquid contacting reaction tank is lower than the lower part without preventing the carrier particles from flowing out without the need for an increase in the bubble diameter which causes such a decrease in the wastewater treatment effect. It is formed to have a large cross-sectional area, and a gas-liquid separation wall with a lower cross-sectional area larger than the lower cross-sectional area of the lower part of the tank is arranged in the widened part of the reaction tank to prevent carrier particles from flowing out into the treated water. The disclosed technique is disclosed.
上記公報の240頁右下欄13〜17行には,「固液分離部1
1内に入り込んだ粒状担体は界面を形成し流動状態にな
り,一部の粒状担体は沈降し,希薄相10の空間内に戻
り,気泡の巻き上げがないので粒状担体の流出は全く起
こらない」と記載されている。The lower right column on page 240, lines 13 to 17 of the above-mentioned publication describes “solid-liquid separation unit 1”.
The granular carriers that have entered into 1 form an interface and become fluidized, and some of the granular carriers settle, return to the space of the dilute phase 10, and there is no bubble up, so no outflow of the granular carriers occurs. " It is described.
しかしながら,この技術の方法の気固液の分離は,前
記の気液分離筒内の液表面での自然な分離にまかせてい
るだけなので,担体粒子に付着した大きな気泡は上記液
表面で自然に分離されるであろうが,担体粒子に付着し
た微細な多数の小気泡は液表面で自然分離を起こし難
い。その上,この廃水処理装置では槽内の流動層濃厚相
6で下方から上昇してくる気泡が常時衝突を起こしてお
り,流動層濃厚相では完全な乱流状態が生じており,そ
の結果,担体粒子には大きな気泡のみならず,無数の小
気泡が付着することになる。そして,この無数の小気泡
が付着した担体粒子が上昇しても邪魔板などに衝突して
そのショックで小気泡が離脱する機会が全くないので,
固液分離部11内に入り込んだ粒状担体は処理水と共に装
置外へ流出してしまうことになる。However, the gas-solid separation in the method of this technique is only left to the natural separation on the liquid surface in the gas-liquid separation cylinder, so that large bubbles adhering to the carrier particles are naturally generated on the liquid surface. Although they will be separated, a large number of fine small bubbles attached to the carrier particles are unlikely to cause spontaneous separation on the liquid surface. In addition, in this wastewater treatment apparatus, bubbles rising from below in the fluidized bed rich phase 6 in the tank constantly collide, and a completely turbulent state occurs in the fluidized bed rich phase. Not only large bubbles but also countless small bubbles adhere to the carrier particles. Even if the carrier particles with the innumerable small bubbles attached rise, there is no chance that the small bubbles will break off due to the collision with a baffle plate or the like.
The granular carrier that has entered the solid-liquid separation section 11 flows out of the apparatus together with the treated water.
本発明は,上記の従来の問題点を解決しようとするも
ので,簡単に安価につくような構成で担体粒子の流出を
効果的に防止し,安定した処理を行うことの可能な廃水
処理装置を提供することを目的とする。SUMMARY OF THE INVENTION The present invention is intended to solve the above-mentioned conventional problems, and a wastewater treatment apparatus capable of effectively preventing the outflow of carrier particles and performing a stable treatment with a simple and inexpensive configuration. The purpose is to provide.
上記に鑑み為された本発明は,微生物の付着に供する
粒状担体を収納する生物処理槽と,該生物処理槽に処理
すべき廃水を供給する原水供給管と,前記生物処理槽の
下部に酸素含有気体を供給する散気口を有する散気管と
を有し,前記生物処理槽内に,粒状担体,水,気体から
なる三相流動層を生じさせて廃水処理を行う流動生物処
理型の廃水処理装置において,前記散気口を,前記生物
処理槽の中央底部に配置し,その上方に前記三相流動層
の流動を整流化せしめるドラフト管を設け,更に該ドラ
フト管の上方の水中に,ドラフト管の上部開口より大き
い面積で周辺が下部に盆状に緑どられた形状の邪魔板を
配置し,該邪魔板の中央部の上方に処理水取り出し口を
設け,前記原水供給管の吐出口を前記邪魔板より低い位
置に配置したことを特徴とする廃水処理装置を要旨とす
る。SUMMARY OF THE INVENTION In view of the above, the present invention provides a biological treatment tank for accommodating a particulate carrier for the attachment of microorganisms, a raw water supply pipe for supplying wastewater to be treated to the biological treatment tank, and an oxygen supply pipe at a lower portion of the biological treatment tank. A diffuser tube having a diffuser port for supplying a contained gas, and a fluidized biological treatment type wastewater in which a three-phase fluidized bed composed of a particulate carrier, water and gas is generated in the biological treatment tank to treat the wastewater. In the treatment apparatus, the air diffuser is disposed at a central bottom of the biological treatment tank, and a draft pipe for rectifying the flow of the three-phase fluidized bed is provided above the air diffuser, and further, in water above the draft pipe, A baffle plate having an area larger than the upper opening of the draft tube and having a lower part surrounded by a tray-like green at the bottom is disposed, a treated water outlet is provided above the center of the baffle plate, and a discharge port of the raw water supply pipe is provided. That the outlet is located lower than the baffle And gist wastewater treatment device according to symptoms.
上記構成の廃水処理装置において,ドラフト管の下部
に配置した散気口からの気体供給により,ドラフト管内
にエアリフト作業による気固液混合物の上向流が生じ,
この上向流がドラフト管上方の邪魔板に衝突し,気液分
離が促進され,且つ粒状担体に付着した小気泡が分離さ
れ,その後,粒状担体はドラフト管の上部開口よりも大
きい面積の邪魔板でドラフト管外に案内され,且つ邪魔
板周辺の盆状に緑どられた部分で下方に向けられ,ドラ
フト管と槽壁間の下向流となる。これにより,系内に安
定した循環流が生じ,廃水の効率のよい処理が行われ
る。また,粒状担体は,邪魔板に衝突した後,ドラフト
管外を下向きに流れるため,邪魔板よりも高い位置の水
中には粒状担体がほとんど含まれておらず,特に,邪魔
板の中央部の上の水中には粒状担体が含まれておらず,
従って,この位置に設けられている処理水取り出し口か
ら処理水を取り出すことにより,粒状担体の流出が防止
される。更に,原水供給管の吐出口を前記邪魔板より低
い位置に配置したことにより,槽内に供給される廃水が
直接処理水取り出し口に流れることがなく,また槽内の
流動系を安定させることもできる。In the wastewater treatment apparatus having the above-described configuration, the gas supply from the air diffuser arranged at the lower part of the draft pipe causes an upward flow of the gas-solid mixture by an air lift operation in the draft pipe,
This upward flow collides with a baffle plate above the draft tube, which promotes gas-liquid separation and separates small air bubbles adhering to the granular carrier, after which the granular carrier has a larger area than the upper opening of the draft tube. It is guided outside the draft tube by the plate, and is directed downward at a basin-shaped green part around the baffle plate, resulting in a downward flow between the draft tube and the tank wall. Thereby, a stable circulation flow is generated in the system, and efficient treatment of wastewater is performed. In addition, since the granular carrier flows downward through the outside of the draft tube after colliding with the baffle plate, the water at a higher position than the baffle plate hardly contains the granular carrier, and in particular, the central portion of the baffle plate The above water does not contain particulate carriers,
Therefore, by taking out the treated water from the treated water outlet provided at this position, the outflow of the granular carrier is prevented. Further, by disposing the discharge port of the raw water supply pipe at a position lower than the baffle plate, the wastewater supplied into the tank does not flow directly to the treated water discharge port, and the flow system in the tank is stabilized. Can also.
以下,図面に示す本発明の実施例を説明する。 Hereinafter, embodiments of the present invention shown in the drawings will be described.
第1図は本発明の一実施例による廃水処理装置の断面
図,第2図はその上面図である。同図において,三相流
動層式廃水処理装置1は,生物処理槽2と,処理すべき
廃水を生物処理槽2に供給する原水供給管3と,生物処
理槽2の下部に酸素含有気体,例えば空気を供給する散
気口4Aを有する散気管4とを有しており,生物処理槽2
内には微生物の付着に供する粒状担体5が収納されてい
る。散気口4Aは,生物処理槽2の中央底部に配置されて
いる。生物処理槽2の中央部には,散気口4Aの上方にな
るように,且つ上端が液中に没する形でドラフト管6が
設けられており,更に,ドラフト管6の上方にドラフト
管の上部開口より大きい面積の邪魔板7が水中に位置す
るように配置されている。この邪魔板7の周辺は下部に
盆状に緑どられた形状をなしており,邪魔板7の周縁7A
はドラフト管6の外側で下方に傾斜している。邪魔板7
の上方には,流出管8が設けられ,その先端の処理水取
り出し口8Aは,邪魔板7の上部中央に位置している。一
方,原水供給管3の吐出口3Aは,邪魔板7より低い位置
でドラフト管6の外側に配置されている。FIG. 1 is a sectional view of a wastewater treatment apparatus according to one embodiment of the present invention, and FIG. 2 is a top view thereof. In FIG. 1, a three-phase fluidized-bed wastewater treatment apparatus 1 includes a biological treatment tank 2, a raw water supply pipe 3 for supplying wastewater to be treated to the biological treatment tank 2, and an oxygen-containing gas at a lower portion of the biological treatment tank 2. For example, it has an air diffuser 4 having an air diffuser 4A for supplying air.
A granular carrier 5 for adhering microorganisms is accommodated therein. The air diffuser 4A is arranged at the central bottom of the biological treatment tank 2. A draft pipe 6 is provided at the center of the biological treatment tank 2 so as to be above the air diffusion port 4A and to have an upper end immersed in the liquid. A baffle plate 7 having an area larger than the upper opening of is disposed underwater. The periphery of the baffle plate 7 is shaped like a tray-shaped green at the bottom, and the periphery 7A of the baffle plate 7
Is inclined downward outside the draft tube 6. Baffle board 7
Above the baffle plate 7, an outflow pipe 8 is provided, and a treated water outlet 8A at the end thereof is located at the upper center of the baffle plate 7. On the other hand, the discharge port 3A of the raw water supply pipe 3 is disposed outside the draft pipe 6 at a position lower than the baffle plate 7.
次に,上記構成の廃水処理装置1の動作を説明する。
原水供給管3で供給され,生物処理槽2内に溜まった廃
水中に散気口4から空気を散気することにより,粒状担
体5が懸濁され,固体,気体,液体の三相流動体が形成
される。この三相流動体は,散気口4Aからの空気による
エアリフト作用によってドラフト管6内を上向流となっ
て流動する。粒状担体5はその表面に活性汚泥を有し,
気体と接触を繰り返すことにより,廃水を浄化する。上
向きに流動された三相流動体はドラフト管6の上部に設
置された邪魔板7に衝突することによって,一部は気体
が分離され,特に粒状担体に付着していた微小な気泡が
分離され,粒状担体及び廃水が流れ方向を規制されるこ
とにより,ドラフト管6と生物処理槽2の間を下向流と
なって生物処理槽2の下部に戻り,この時,原水供給管
3により供給される流入水をまき込み,散気口4Aにより
再び攪拌される。このようにして,生物処理槽2内には
矢印で示す循環流が安定して形成される。汚泥をその表
面に有する粒状担体5はこの過程で気液と接触を繰り返
し,廃水を浄化する。粒状担体5と分離された処理水
は,邪魔板7の上部から流出管8によって次工程に導か
れる。これによって流出水9には,粒状担体5が含まれ
ることなく,処理を安定して行うことができる。Next, the operation of the wastewater treatment apparatus 1 having the above configuration will be described.
By diffusing air from the air diffuser 4 into the wastewater supplied by the raw water supply pipe 3 and stored in the biological treatment tank 2, the particulate carrier 5 is suspended, and a three-phase fluid of solid, gas, and liquid Is formed. This three-phase fluid flows upward in the draft pipe 6 due to the air lift effect of the air from the air diffuser 4A. The granular carrier 5 has activated sludge on its surface,
Purify wastewater by repeating contact with gas. The upwardly flowing three-phase fluid collides with a baffle plate 7 provided above the draft tube 6, whereby a part of the gas is separated, and in particular, fine bubbles adhering to the granular carrier are separated. The flow direction of the granular carrier and the wastewater is regulated, so that a downward flow flows between the draft pipe 6 and the biological treatment tank 2 to return to the lower part of the biological treatment tank 2, and at this time, the raw water is supplied by the raw water supply pipe 3. The incoming inflow water is swirled and is again stirred by the air diffuser 4A. In this way, a circulating flow indicated by an arrow is stably formed in the biological treatment tank 2. The granular carrier 5 having sludge on its surface repeats contact with gas and liquid in this process to purify wastewater. The treated water separated from the granular carrier 5 is guided to the next step from the upper part of the baffle plate 7 by the outflow pipe 8. As a result, the effluent 9 can be stably processed without containing the granular carrier 5.
第3図は本発明の他の実施例による廃水処理装置の断
面図,第4図はその上面図である。第3図,第4図の実
施例では,邪魔板7の上部に,下端に処理水取り出し口
11Aを備えたエアリフト管11と,そのエアリフト管11に
エアリフト用の空気を供給する空気管12を設けたもので
あり,他の構成は第1図,第2図の実施例と同様であ
る。第3図,第4図の実施例では,エアリフト管11によ
って,処理水を生物処理槽2の液面よりも高い位置に排
出することができる。FIG. 3 is a sectional view of a wastewater treatment apparatus according to another embodiment of the present invention, and FIG. 4 is a top view thereof. 3 and 4, in the upper part of the baffle plate 7 and at the lower end the treated water outlet.
An air lift tube 11 having an air lift tube 11A and an air tube 12 for supplying air for air lift to the air lift tube 11 are provided. The other structure is the same as that of the embodiment shown in FIGS. In the embodiment shown in FIGS. 3 and 4, the treated water can be discharged to a position higher than the liquid level of the biological treatment tank 2 by the air lift pipe 11.
以上に説明したように,本発明は三相流動層型の廃水
処理装置において,ドラフト管の上方の水中に邪魔板を
配置するという簡単な構成によって,生物処理槽内にド
ラフト管の内外を通る安定した循環流を発生させること
ができ,廃水を効率良く処理することができると共に,
廃水処理に利用した粒状担体を処理水から効率的に分離
することができ,処理効率が低下しない等の効果を有し
ている。また,本発明の装置では,粒状担体が処理水に
ほとんど同伴しないため,次工程に流出粒状担体を捕集
するための沈澱槽,捕集した粒状担体,汚泥等を返送す
る設備が不要で経済的である等の効果も有している。As described above, the present invention relates to a three-phase fluidized bed type wastewater treatment apparatus, in which a baffle plate is disposed in water above a draft tube, and the wastewater treatment device passes through the inside and outside of the draft tube in the biological treatment tank. A stable circulation flow can be generated, and wastewater can be treated efficiently.
The granular carrier used for wastewater treatment can be efficiently separated from the treated water, and the treatment efficiency is not reduced. Further, in the apparatus of the present invention, since the granular carrier hardly accompanies the treated water, there is no need for a settling tank for collecting the effluent granular carrier, a facility for returning the collected granular carrier, sludge, etc. in the next step, which is economical. It also has the effect of being a target.
第1図は本発明の一実施例による廃水処理装置の断面
図,第2図はその上面図,第3図は本発明の他の実施例
による廃水処理装置の断面図,第4図はその上面図であ
る。 1……廃水処理装置,2……生物処理槽,3……原水供給
管,3A……吐出口,4……散気管,4A……散気口,5……粒状
担体,6……ドラフト管,7……邪魔板,8……流出管,8A…
…処理水取り出し口,9……処理水,11……エアリフト管,
11A……処理水取り出し口,12……空気管。1 is a sectional view of a wastewater treatment apparatus according to one embodiment of the present invention, FIG. 2 is a top view thereof, FIG. 3 is a sectional view of a wastewater treatment apparatus according to another embodiment of the present invention, and FIG. It is a top view. 1 wastewater treatment equipment, 2 biological treatment tank, 3 raw water supply pipe, 3A discharge port, 4 diffuser pipe, 4A diffuser port, 5 granular carrier, 6 draft Tube, 7… Baffle plate, 8… Outflow tube, 8A…
… Treated water outlet, 9… treated water, 11… air lift tube,
11A ... treated water outlet, 12 ... air tube.
───────────────────────────────────────────────────── フロントページの続き (56)参考文献 実公 昭60−17271(JP,Y2) ──────────────────────────────────────────────────続 き Continuation of the front page (56) Reference Jikken Sho 60-17271 (JP, Y2)
Claims (1)
生物処理槽と,該生物処理槽に処理すべき廃水を供給す
る原水供給管と,前記生物処理槽の下部に酸素含有気体
を供給する散気口を有する散気管とを有し,前記生物処
理槽内に,粒状担体,水,気体からなる三相流動層を生
じさせて廃水処理を行う流動生物処理型の廃水処理装置
において,前記散気口を,前記生物処理槽の中央底部に
配置し,その上方に前記三相流動層の流動を整流化せし
めるドラフト管を設け,更に該ドラフト管の上方の水中
に,ドラフト管の上部開口より大きい面積で周辺が下部
に盆状に緑どられた形状の邪魔板を配置し,該邪魔板の
中央部の上方に処理水取り出し口を設け,前記原水供給
管の吐出口を前記邪魔板より低い位置に配置したことを
特徴とする廃水処理装置。1. A biological treatment tank for accommodating a granular carrier for the attachment of microorganisms, a raw water supply pipe for supplying wastewater to be treated to the biological treatment tank, and an oxygen-containing gas supplied to a lower portion of the biological treatment tank. A fluid biological treatment type wastewater treatment apparatus having a diffuser tube having an air diffuser port and generating a three-phase fluidized bed composed of a particulate carrier, water, and gas in the biological treatment tank to perform wastewater treatment; An air diffuser is disposed at the central bottom of the biological treatment tank, and a draft pipe for rectifying the flow of the three-phase fluidized bed is provided above the air diffuser, and an upper opening of the draft pipe is provided in water above the draft pipe. A baffle plate having a larger area and a perimeter shaped like a tray at the bottom is disposed, and a treated water outlet is provided above a central portion of the baffle plate, and a discharge port of the raw water supply pipe is connected to the baffle plate. Wastewater treatment facility characterized by being located at a lower position Apparatus.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP25808988A JP2579295B2 (en) | 1988-10-13 | 1988-10-13 | Wastewater treatment equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP25808988A JP2579295B2 (en) | 1988-10-13 | 1988-10-13 | Wastewater treatment equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH02102792A JPH02102792A (en) | 1990-04-16 |
| JP2579295B2 true JP2579295B2 (en) | 1997-02-05 |
Family
ID=17315360
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP25808988A Expired - Fee Related JP2579295B2 (en) | 1988-10-13 | 1988-10-13 | Wastewater treatment equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2579295B2 (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH06343987A (en) * | 1993-06-08 | 1994-12-20 | Ngk Insulators Ltd | Waste water treatment device using microbe carrier |
| DE10026867B4 (en) * | 2000-05-31 | 2005-06-02 | Mester, Thomas, Dipl.-Ing. | Reactor and process for wastewater treatment |
| KR100399295B1 (en) * | 2001-07-23 | 2003-09-26 | 삼성에버랜드 주식회사 | Reactor installed in baffle |
| CN115367917B (en) * | 2022-08-19 | 2023-07-25 | 四川发展环境科学技术研究院有限公司 | Multi-mode water treatment device and treatment method thereof |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6017271U (en) * | 1983-07-15 | 1985-02-05 | トリニテイ工業株式会社 | painting equipment |
-
1988
- 1988-10-13 JP JP25808988A patent/JP2579295B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH02102792A (en) | 1990-04-16 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US6811690B2 (en) | Method and apparatus for mixing fluids, separating fluids, and separating solids from fluids | |
| JP5665307B2 (en) | Organic waste water treatment apparatus and organic waste water treatment method | |
| KR102145037B1 (en) | Rapid float filtration device | |
| JP2002159990A (en) | Anaerobic treating vessel | |
| JP2579295B2 (en) | Wastewater treatment equipment | |
| JP2606690B2 (en) | Vertical loop type reaction tank with air release delay characteristics | |
| US6773596B2 (en) | Activated sludge method and device for the treatment of effluent with nitrogen and phosphorus removal | |
| JPH07308686A (en) | Upward flow anaerobic treatment device | |
| US5364530A (en) | Process for the biological purification of sewage | |
| JP2544712B2 (en) | Wastewater treatment facility | |
| JP2000140883A (en) | Primary treatment of organic sewage and device therefor | |
| JP2577673B2 (en) | Sewage treatment tank | |
| JP3169117B2 (en) | Biological wastewater treatment equipment | |
| JP2544713B2 (en) | Wastewater treatment equipment | |
| JPH05285493A (en) | Sewage treatment apparatus | |
| JP4342687B2 (en) | Wastewater treatment equipment | |
| JPS6223596Y2 (en) | ||
| JP2000176477A (en) | Treatment of highly contaminated sewage by using microorganism-immobilized carrier, treating device therefor, and carrier separating device | |
| JPH10216787A (en) | Wastewater treatment equipment | |
| JPS62136295A (en) | Wastewater treatment method and device | |
| JP2001047085A (en) | Anaerobic wastewater treatment equipment | |
| JP7712803B2 (en) | Wastewater treatment device and wastewater treatment method | |
| JPH0127916Y2 (en) | ||
| JPH02135196A (en) | Sewage water treatment equipment | |
| SU1632952A1 (en) | Apparatus for biological purification of effluents |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| LAPS | Cancellation because of no payment of annual fees |