JPH0683831B2 - Sewage treatment method - Google Patents
Sewage treatment methodInfo
- Publication number
- JPH0683831B2 JPH0683831B2 JP1015760A JP1576089A JPH0683831B2 JP H0683831 B2 JPH0683831 B2 JP H0683831B2 JP 1015760 A JP1015760 A JP 1015760A JP 1576089 A JP1576089 A JP 1576089A JP H0683831 B2 JPH0683831 B2 JP H0683831B2
- Authority
- JP
- Japan
- Prior art keywords
- water
- treated
- draft tube
- contact
- membrane
- 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 - Lifetime
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)
- Separation Using Semi-Permeable Membranes (AREA)
Description
【発明の詳細な説明】 (産業上の利用分野) 本発明は、好気性生物による都市下水や産業廃水に浄化
処理を施す汚水処理方法に関する。TECHNICAL FIELD The present invention relates to a sewage treatment method for purifying urban sewage or industrial wastewater by aerobic organisms.
(従来の技術) 一般に活性汚泥法や接触ばっき気法などの好気性の汚水
処理法においては、反応槽の後に沈殿槽を設けて固液の
分離を行い、清澄な処理水を得るようにしている。(Prior art) Generally, in aerobic sewage treatment methods such as the activated sludge method and contact aeration method, a precipitation tank is installed after the reaction tank to separate solid and liquid to obtain clear treated water. ing.
近年、沈殿槽にかえて精密濾過や限外濾過などの高分子
膜を用いた膜濾過装置を用いて、非常に清澄度の高い処
理水を確実に得られる処理方式が知られている。In recent years, there has been known a treatment method that can reliably obtain treated water with extremely high clarity by using a membrane filtration device using a polymer membrane such as microfiltration or ultrafiltration instead of a settling tank.
また、特公昭48-40971号公報または特開昭62-68599号公
報に記載されているように、被処理水を膜濾過装置まで
循環させる循環路を形成し、この循環路を循環する被処
理水を濾過する方法が知られている。Further, as described in JP-B-48-40971 or JP-A-62-68599, a circulation path for circulating water to be treated to a membrane filtration device is formed, and a treatment object circulating in the circulation path is formed. Methods of filtering water are known.
(発明が解決しようとする課題) 上述のような膜濾過装置を用いる処理方法の主要な問題
点の一つは、分離に要するエネルギーが大きいことで、
分離膜の表面に浮遊物やコロイドなどの粒子が蓄積して
濾過速度が著しく低下することを防ぐためには、常に分
離膜表面に非常に大きな流速で該分離液を流し続けなが
ら濾過しなければならず、結果として多大のエネルギー
消費をもたらすという問題がある。(Problems to be Solved by the Invention) One of the main problems of the treatment method using the membrane filtration device as described above is that the energy required for separation is large,
In order to prevent particles such as suspended solids and colloids from accumulating on the surface of the separation membrane and significantly reducing the filtration rate, the separation liquid must always be filtered while continuously flowing the separation liquid at a very high flow rate. However, there is a problem that a large amount of energy is consumed as a result.
また、被処理水の処理のために、接触ばっきのための循
環流と別個に濾過用の循環路を形成しなくてはならず、
経済性に欠け、運転コストもかかり、装置が大型となり
高価となる問題を有している。In addition, in order to treat the water to be treated, a circulation path for filtration must be formed separately from the circulation flow for contacting,
There is a problem in that the cost is low, the operating cost is high, and the device is large and expensive.
本発明は上述の問題点に鑑みなされたもので、接触ばっ
きのための循環流を利用して被処理水を濾過し、膜濾過
に必要なエネルギーを少なくして膜濾過によって清澄度
の高い処理水を得る汚水処理方法を提供するものであ
る。The present invention has been made in view of the above-mentioned problems, and the water to be treated is filtered by using a circulating flow for contacting, and the energy required for membrane filtration is reduced to achieve high clarity by membrane filtration. It is intended to provide a sewage treatment method for obtaining treated water.
(課題を解決するための手段) 請求項1の発明の汚水処理方法は、微生物が付着する浸
漬炉床を設けた接触ばっき気槽に導入された被処理水
を、この接触ばっき気槽の水面下に設けられたドラフト
チューブの内部に配設されている散気部からの散気によ
る発生するエアーリフト作用によりこのドラフトチュー
ブ内の上向流と浸漬炉床の下降流とにより循環させて接
触酸化する汚水処理方法であって、前記浸漬濾床の通過
によって接触酸化された被処理水がドラフトチューブを
エアーリフト作用により上向流となって高速で流通する
際、このドラフチューブ内に配設された膜濾過装置の濾
過膜によって濾過され、この濾過された処理水を前記ド
ラフトチューブ内に配設した処理水管により前記接触ば
っき気槽外へ導出するものである。(Means for Solving the Problem) The sewage treatment method of the invention of claim 1 is a method for treating treated water introduced into a contact aeration tank provided with a dipping hearth to which microorganisms adhere, Of the draft tube provided below the water surface of the draft tube is circulated by the upward flow in the draft tube and the downward flow of the immersion hearth by the air lift action generated by the diffuser. A method for treating sewage by contact oxidation, in which the water to be treated that has been contact-oxidized by passing through the submerged filter bed flows into the draft tube at a high speed as an upward flow due to the air lift action, The treated water is filtered by a filtration membrane of a membrane filtration device provided, and the filtered treated water is led out of the contact aeration tank by a treated water pipe provided in the draft tube.
請求項2記載の汚水処理方法は、微生物が付着する浸漬
炉床を設けた接触ばっき気槽に導入された被処理水を、
液ポンプにより前記接触ばっき気槽の上部に連通させた
循環管から前記接触ばっき気槽に上端を水面に突出させ
て設けたドラフトチューブを通して浸漬炉床の下方に流
動させ、前記ドラフトチューブに接続した空気吸入管か
ら吸入した空気により接触酸化させながら被処理水を浸
漬炉床を循環させる汚水処理方法であって、前記循環管
の途中に設けた膜濾過装置の濾過膜にて濾過された処理
水を膜濾過装置に接続した処理水管により前記接触ばっ
き気槽外へ導出するものである。The sewage treatment method according to claim 2, wherein the water to be treated introduced into the contact aeration tank provided with an immersion hearth to which microorganisms adhere is
From the circulation pipe connected to the upper part of the contact aeration tank by a liquid pump, flow through the draft tube provided with the upper end protruding to the water surface to the contact aeration tank to the bottom of the dipping hearth, and to the draft tube. A sewage treatment method in which water to be treated is circulated in a dipping hearth while being contact-oxidized by air sucked from a connected air suction pipe, and is filtered by a filtration membrane of a membrane filtration device provided in the middle of the circulation pipe. The treated water is led out of the contact aeration tank by a treated water pipe connected to a membrane filtration device.
(作用) 請求項1記載の発明の汚水処理方法は、被処理水は、ド
ラフトチューブに発生するエアリフト作用によって微生
物の付着する接触濾材を充填する浸漬炉床を汚泥物質を
濾過され、微生物によって酸化分解されながら循環す
る。この循環途中のドラフトチューブに設けた膜濾過装
置の濾過膜で被処理水は濾過処理され、被処理水を濾過
するために被処理水の濾過循環路を必要とせず、また、
前記浸漬炉床によって大部分の汚濁物質が除去され、ま
た、ドラフトチューブを流れる被処理水は高速流のた
め、膜濾過装置の膜面を流通し膜面を洗浄するとともに
膜を透過した処理水は、処理水管より接触ばっき気槽外
に導出される。(Operation) In the sewage treatment method of the invention according to claim 1, in the treated water, the sludge substance is filtered by the submerged hearth filled with the contact filter medium to which microorganisms adhere due to the air lift action generated in the draft tube, and the water is oxidized by the microorganisms. Circulates while being decomposed. The treated water is filtered by the filtration membrane of the membrane filtration device provided in the draft tube in the middle of this circulation, and a filtration circulation path for the treated water is not required to filter the treated water.
Most of the contaminants are removed by the immersion hearth, and the water to be treated flowing through the draft tube is a high-speed flow, so the treated water that has passed through the membrane surface of the membrane filtration device and washed the membrane surface and has permeated the membrane. Is discharged from the treated water pipe to the outside of the tank.
請求項2の発明の汚水処理方法は、被処理水が液ポンプ
によって空気吸入管に接続したドラフトチューブを通過
する際に空気を吸入して浸漬濾床を循環され、この浸漬
濾床を通過しながら酸化分解されながら循環する被処理
水はこの循環途中にて膜濾過装置の濾過膜にて濾過処理
するため、濾過処理ための循環路を必要とせず、前記浸
漬炉床によって大部分の汚濁物質が除去され、また、ド
ラフトチューブに連結した循環管中を流れる被処理水の
高速流が膜濾過装置の濾過膜の膜面を流通して膜面を洗
浄し、濾過膜を通過した処理水は接触ばっき気槽外へ導
出される。In the sewage treatment method of the invention of claim 2, when the water to be treated passes through a draft tube connected to an air suction pipe by a liquid pump, air is sucked in to be circulated in the submerged filter bed and passed through the submerged filter bed. While the water to be circulated while being oxidatively decomposed is filtered by the filtration membrane of the membrane filtration device in the course of this circulation, a circulation path for the filtration treatment is not required, and most of the pollutants by the immersion hearth In addition, the high-speed flow of the water to be treated flowing through the circulation pipe connected to the draft tube flows through the membrane surface of the filtration membrane of the membrane filtration device to wash the membrane surface, and the treated water that has passed through the filtration membrane is It is discharged from the contact tank.
(実施例) 本発明の汚水処理方法の一実施例を第1図に示す汚水処
理装置について説明する。(Example) An example of the sewage treatment method of the present invention will be described with respect to the sewage treatment apparatus shown in FIG.
1は接触ばっき気槽で、中心に上下開口面を被処理水中
で開口させたドラフトチューブ2が直立され、このドラ
フトチューブ2の周囲に微生物が付着する接触濾材を充
填した浸漬炉床3が形成されている。Reference numeral 1 is a contact aeration tank, in which a draft tube 2 having upper and lower open surfaces opened in the water to be treated is erected upright, and an immersion hearth 3 filled with a contact filter medium on which microorganisms adhere is provided around the draft tube 2. Has been formed.
このドラフトチューブ2内には空気を送り込む散気管4
を連通させた散気部、すなわち散気頭5が配設されてい
る。また、この散気部の下方に位置して前記ドラフトチ
ューブ2内には濾過膜を有する膜濾過装置6が挿入され
ている。An air diffuser 4 for feeding air into the draft tube 2
An air diffusing portion communicating with each other, that is, an air diffusing head 5 is provided. Further, a membrane filtration device 6 having a filtration membrane is inserted into the draft tube 2 located below the air diffuser.
また、前記膜濾過装置6は浸透膜からなる濾過膜で形成
された中空密閉体で構成され、この膜濾過装置6に処理
水管7が連通され、処理水管7はドラフトチューブ2よ
り引出されて接触ばっき気槽1の外部に導出されてい
る。Further, the membrane filtration device 6 is composed of a hollow closed body formed of a filtration membrane made of a permeation membrane, and the treated water pipe 7 is communicated with the membrane filtration device 6, and the treated water pipe 7 is drawn out from the draft tube 2 and brought into contact therewith. It is led to the outside of the air tank 1.
次に、この汚水処理装置により実施される汚水処理方法
の一実施例を説明する。Next, an example of a sewage treatment method implemented by this sewage treatment apparatus will be described.
接触ばっき気槽1に被処理水を導入し、ドラフトチュー
ブ2中に散気管4の散気頭5から空気を導入して散気す
ると、被処理水はエアリフト作用によりドラフトチュー
ブ2中で上向流が生じ、ドラフトチューブ2の上端より
流出して微生物が付着した接触濾材を充填した浸漬炉床
3の上側に流動され、被処理水は下降流となって浸漬炉
床3を濾過されながら流動して接触酸化され再びドラフ
トチューブ2の下端より上昇して、接触ばっき気槽1内
を接触酸化させながら循環する。When the water to be treated is introduced into the contact aeration tank 1 and the air is introduced into the draft tube 2 from the air diffusing head 5 of the air diffuser 4, the water to be treated rises in the draft tube 2 due to the air lift action. A countercurrent is generated, flows out from the upper end of the draft tube 2 and is flowed to the upper side of the immersion hearth 3 filled with the contact filter medium on which the microorganisms are adhered, and the water to be treated becomes a downward flow while filtering the immersion hearth 3. It flows, is contact-oxidized, rises again from the lower end of the draft tube 2, and circulates in the contact aeration tank 1 while contact-oxidizing.
また、ドラフトチューブ2内の膜濾過装置6は表面を高
速で流通する被処理水によって常に洗浄され表面に浸漬
炉床3での濾過残の浮遊物やコロイドなどの汚濁物質が
付着することがなく、濾過膜の濾過作用が有効に進行す
る。膜濾過装置6内に浸透した清澄な処理水は、処理水
管7によって外部へ排出される。Further, the membrane filtration device 6 in the draft tube 2 is constantly washed with the water to be treated flowing at a high speed on the surface, so that the floating residue of the filtration residue in the immersion hearth 3 and the pollutants such as colloids do not adhere to the surface. The filtration action of the filtration membrane effectively proceeds. The clear treated water that has penetrated into the membrane filtration device 6 is discharged to the outside by the treated water pipe 7.
次に本発明の他の実施例を実施する汚水処理装置を第2
図によって説明する。Next, the second embodiment of the sewage treatment apparatus for carrying out another embodiment of the present invention
It will be described with reference to the drawings.
接触ばっき気槽1に配設したドラフトチューブ2の上端
はこの接触ばっき気槽1の水面より上方に突出され、こ
の接触ばっき気槽1には浸漬炉床3の上方位置で水面よ
り下方に途中に液ポンプ8を有する循環管9が連通され
ている。The upper end of the draft tube 2 arranged in the contact aeration tank 1 is projected above the water surface of the contact aeration tank 1, and the contact tube 1 is located above the immersion hearth 3 above the water surface. A circulation pipe 9 having a liquid pump 8 in the middle is communicated downward.
また、前記循環管9は前記接触ばっき気槽1よりも上方
に突出した前記ドラフトチューブ2に連通されている。
そして、前記液ポンプ8とドラフトチューブ2との間に
位置して前記循環管9の途中には径大部10が形成され、
この径大部10には膜濾過装置6が挿入され、この膜濾過
装置6は浸透膜からなる濾過膜で形成された中空密閉体
で構成され、この膜濾過装置6に処理水管7が連通され
ている。Further, the circulation pipe 9 is communicated with the draft tube 2 protruding above the contact aeration tank 1.
A large diameter portion 10 is formed in the middle of the circulation pipe 9 located between the liquid pump 8 and the draft tube 2,
A membrane filtration device 6 is inserted into the large-diameter portion 10, and the membrane filtration device 6 is composed of a hollow closed body formed of a permeation membrane filtration membrane, and the treated water pipe 7 is connected to the membrane filtration device 6. ing.
さらに、前記ドラフトチューブ2の上端開口部からは軸
方向に空気吸入管11が挿入され、この空気吸入管11の先
端は循環管9の開口部12よりも稍下方でノズル状に開口
されている。Further, an air suction pipe 11 is axially inserted from the upper end opening of the draft tube 2, and the tip of the air suction pipe 11 is opened in a nozzle shape slightly below the opening 12 of the circulation pipe 9. .
次に、この汚水処理装置によって本発明の他の実施例を
説明する。Next, another embodiment of the present invention will be described using this sewage treatment apparatus.
接触ばっき気槽1に導入された被処理水は、浸漬炉床3
の上部から液ポンプ8で汲み上げられ循環管9によって
ドラフトチューブ2の上部に供給され、ドラフトチュー
ブ2を流下して浸漬炉床3の下部に吐出され、微生物の
付着する接触濾材を充填した浸漬炉床3を被処理水中の
浮遊する汚濁物質を濾過され、微生物によって酸化分解
されながら上昇して再び浸漬炉床3の上方より液ポンプ
8によって吸い上げられ、ドラフトチューブ2に導入さ
れて循環する。The water to be treated introduced into the contact aeration tank 1 is the immersion hearth 3
Is fed from the upper part of the liquid pump 8 by the liquid pump 8 to the upper part of the draft tube 2 by the circulation pipe 9, and the draft tube 2 is flowed down and discharged to the lower part of the dipping hearth 3 to be filled with a contact filter medium to which microorganisms adhere. Floating pollutants in the water to be treated are filtered from the floor 3, rise as they are oxidatively decomposed by microorganisms, and are sucked up again from above the immersion furnace floor 3 by the liquid pump 8 and introduced into the draft tube 2 for circulation.
そして、ドラフトチューブ2の上部に挿入された空気流
入管11の先端ノズル状の開口部は、ドラフトチューブ2
の下降する水流によって負圧が生じ空気を吸入して、ド
ラフトチューブ2の被処理水中に微生物によって酸化分
解させるために、強制的に空気を供給する。The tip nozzle-shaped opening of the air inflow pipe 11 inserted into the upper portion of the draft tube 2 is
A negative pressure is generated by the descending water flow and the air is sucked, and the air is forcibly supplied to the water to be treated in the draft tube 2 for oxidative decomposition by the microorganisms.
また、膜濾過装置6内に浸透圧によって浸透した清澄な
処理水は、処理水管7によって接触ばっき気槽1の外方
に導出される。Further, the clarified treated water that has penetrated into the membrane filtration device 6 by the osmotic pressure is drawn out of the contact aeration tank 1 by the treated water pipe 7.
さらに、膜濾過装置6は被処理水が液ポンプ8で高速で
送られる循環管9の径大部10内に位置するため浸透膜の
外面が洗い流され、浸漬炉床3での濾過残の浮遊物やコ
ロイドなどの汚濁物質の付着が防止される。Further, since the membrane filtration device 6 is located in the large diameter portion 10 of the circulation pipe 9 through which the water to be treated is fed at a high speed by the liquid pump 8, the outer surface of the permeation membrane is washed away, and the filtration residue on the immersion hearth 3 floats. The attachment of pollutants such as objects and colloids is prevented.
次に、前記第2図に示す膜濾過装置6は第3図に示すよ
うに、被処理水が強制的に流通される循環管9の途中に
膜濾過装置6の両端を連通させて挿入して、この膜濾過
装置6を密封包囲した外套体13から処理水管7を導出さ
せることもできる。Next, as shown in FIG. 3, the membrane filtration device 6 shown in FIG. 2 is inserted by inserting both ends of the membrane filtration device 6 in the middle of the circulation pipe 9 through which the water to be treated is forced to flow. Then, the treated water pipe 7 can be led out from the outer casing 13 that hermetically surrounds the membrane filtration device 6.
この第3図に示す膜濾過装置6は、浸透濾過された処理
水が膜濾過装置6の外面に浸出し、外套体13内に溜った
処理水が処理水管7によって導出される。In the membrane filtration device 6 shown in FIG. 3, the treated water that has been permeated and filtered permeates the outer surface of the membrane filtration device 6, and the treated water that has accumulated in the outer casing 13 is led out by the treated water pipe 7.
(発明の効果) 請求項1記載の発明によれば、被処理水は、エアリフト
により強制的に流通させるドラフトチューブによって循
環され、浸漬炉床を被処理水中に浮遊する汚濁物質を濾
過され、接触濾材に付着する微生物によって酸化分解さ
れながら循環し、その循環途中で被処理水が高速に流通
する位置に膜濾過装置を設けて濾過されるため、膜濾過
装置は常時速度を有する被処理水中に曝されているか
ら、被処理水との接触面は洗い流され濾過膜の表面に浮
遊物やコロイドが付着するのを防止され、濾過効果を高
めることができる。また、膜濾過のために別途の循環路
を形成する必要もなく、膜濾過装置の洗浄のために、高
速分離水を流すためのエネルギーを別に必要としないか
ら運転コストもかからず、経済上有利であり、また、装
置全体も小型にできる。(Effect of the invention) According to the invention of claim 1, the water to be treated is circulated by the draft tube which is forced to flow by the air lift, and the pollutants floating in the water to be treated are filtered through the immersion hearth and contacted. It circulates while being oxidatively decomposed by the microorganisms adhering to the filter medium, and a membrane filtration device is installed at a position where the water to be treated circulates at a high speed in the middle of the circulation, so that the membrane filtration device is always in the water to be treated which has a speed. Since it is exposed, the contact surface with the water to be treated is washed away to prevent floating substances and colloids from adhering to the surface of the filtration membrane, and the filtration effect can be enhanced. In addition, there is no need to form a separate circulation path for membrane filtration, and no additional energy is required to flow the high-speed separated water for cleaning the membrane filtration device, so there is no operating cost and it is economical. This is advantageous, and the entire device can be downsized.
請求項2記載の発明によれば、被処理水は、液ポンプで
強制的に送水される循環管によって循環され、浸漬炉床
を被処理水中に浮遊する汚濁物質を濾過され、接触濾材
に付着する微生物によって酸化分解されながら循環し、
その循環途中で被処理水が高速に流通する位置の膜濾過
装置で濾過されるため、膜濾過装置は常時速度を有する
被処理水中に曝されているから、被処理水との接触面は
洗い流され濾過膜の表面に浮遊物やコロイドが付着する
のを防止され、濾過効果を高めることができる。また、
膜濾過のために別途の循環路を形成する必要もなく、膜
濾過装置の洗浄のために、高速分離水を流すためのエネ
ルギーを別に必要としないから運転コストもかからず、
経済上有利であり、また、装置全体も小型にできる。According to the second aspect of the present invention, the water to be treated is circulated by the circulation pipe forcibly fed by the liquid pump, the pollutants floating in the water to be treated are filtered through the immersion hearth, and adhered to the contact filter medium. Circulates while being oxidatively decomposed by
During the circulation, the water to be treated is filtered by the membrane filtration device at a high-speed position, so the membrane filtration device is constantly exposed to the water to be treated, and the contact surface with the water to be treated is washed away. It is possible to prevent floating substances and colloids from adhering to the surface of the filtration membrane and enhance the filtration effect. Also,
There is no need to form a separate circulation path for membrane filtration, and there is no need for additional energy for flowing the high-speed separated water for cleaning the membrane filtration device, so operating costs are low.
It is economically advantageous, and the entire device can be downsized.
第1図は本発明の汚水処理方法を実施する汚水処理装置
の縦断面図、第2図は本発明の汚水処理方法を実施する
他の汚水処理装置の縦断面図、第3図は第2図に示す膜
濾過装置の他の実施例を示す循環管の一部の縦断面図で
ある。 1……接触ばっき気槽、2……ドラフトチューブ、6…
…膜濾過装置、7……処理水管、8……液ポンプ、9…
…循環管。FIG. 1 is a vertical sectional view of a sewage treatment apparatus for carrying out the sewage treatment method of the present invention, FIG. 2 is a vertical sectional view of another sewage treatment apparatus for carrying out the sewage treatment method of the present invention, and FIG. It is a longitudinal cross-sectional view of a part of a circulation pipe showing another embodiment of the membrane filtration device shown in the figure. 1 ... contact air tank, 2 ... draft tube, 6 ...
... Membrane filter, 7 ... Treatment water pipe, 8 ... Liquid pump, 9 ...
… Circulation pipe.
Claims (2)
っき気槽に導入された被処理水を、この接触ばっき気槽
の水面下に設けられたドラフトチューブの内部に配設さ
れている散気部からの散気による発生するエアーリフト
作用によりこのドラフトチューブ内の上向流と浸漬床
の下降流とにより循環させて接触酸化する汚水処理方法
であって、 前記浸漬濾床の通過によって接触酸化された被処理水が
ドラフトチューブをエアーリフト作用により上向流とな
って高速で流通する際、このドラフトチューブ内に配設
された膜濾過装置の濾過膜によって濾過され、この濾過
された処理水を前記ドラフトチューブ内に配設した処理
水管により前記接触ばっき気槽外へ導出する ことを特徴とする汚水処理方法。1. The water to be treated introduced into a contact aeration tank provided with a submerged bed to which microorganisms adhere is disposed inside a draft tube provided below the water surface of the contact aeration tank. A sewage treatment method of contact oxidation by circulating by the upward flow in the draft tube and the downward flow of the submerged bed by the air lift action generated by the air diffused from the air diffuser which passes through the submerged filter bed. When the water to be treated that has been contact-oxidized by the draft tube flows upward at a high speed due to the air lift action, it is filtered by the filtration membrane of the membrane filtration device arranged in the draft tube, and this filtered water is filtered. The treated water is discharged to the outside of the contact aeration tank by means of a treated water pipe arranged in the draft tube.
っき気槽に導入された被処理水を、液ポンプにより前記
接触ばっき気槽の上部に連通させた循環管から前記接触
ばっ気槽に上端を水面に突出させて設けたドラフトチュ
ーブを通して浸漬床の下方に流動させ、前記ドラフト
チューブに接続した空気吸入管から吸入した空気により
接触酸化させながら被処理水を浸漬床を循環させる汚
水処理方法であって、 前記循環管の途中に設けた膜濾過装置の濾過膜にて濾過
された処理水を膜濾過装置に接続した処理水管により前
記接触ばっき気槽外へ導出する ことを特徴とする汚水処理方法。2. The contact aeration through a circulation pipe in which water to be treated introduced into a contact aeration tank provided with an immersion bed to which microorganisms adhere is communicated to the upper part of the contact aeration tank by a liquid pump. Sewage that circulates the water to be treated while flowing through the draft tube provided with the upper end protruding to the water surface below the immersion bed, and causing the treated water to circulate through the immersion bed while being contact-oxidized by the air sucked from the air suction pipe connected to the draft tube. A treatment method, wherein treated water filtered by a filtration membrane of a membrane filtration device provided in the middle of the circulation pipe is led out of the contact aeration tank by a treatment water pipe connected to the membrane filtration device. Sewage treatment method.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1015760A JPH0683831B2 (en) | 1989-01-25 | 1989-01-25 | Sewage treatment method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1015760A JPH0683831B2 (en) | 1989-01-25 | 1989-01-25 | Sewage treatment method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH02194894A JPH02194894A (en) | 1990-08-01 |
| JPH0683831B2 true JPH0683831B2 (en) | 1994-10-26 |
Family
ID=11897739
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1015760A Expired - Lifetime JPH0683831B2 (en) | 1989-01-25 | 1989-01-25 | Sewage treatment method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0683831B2 (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5656169A (en) * | 1996-08-06 | 1997-08-12 | Uniroyal Chemical Ltd./Ltee | Biodegradation process for de-toxifying liquid streams |
| JP2003024959A (en) * | 2001-07-17 | 2003-01-28 | Fuji Clean Kogyo Kk | Method and apparatus for treating wastewater |
| CN121342188B (en) * | 2025-12-16 | 2026-02-27 | 内蒙古博思达科技有限公司 | Flocculation tank for extracting potato protein |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5337428B2 (en) * | 1971-10-01 | 1978-10-09 | ||
| JPS61120694A (en) * | 1984-11-19 | 1986-06-07 | Mitsubishi Kakoki Kaisha Ltd | Treatment of organic waste water |
| JPS61129094A (en) * | 1984-11-26 | 1986-06-17 | Nitto Electric Ind Co Ltd | Apparatus for treating membrane |
| JPS6268599A (en) * | 1985-09-19 | 1987-03-28 | Kurita Water Ind Ltd | Sewage treatment equipment |
-
1989
- 1989-01-25 JP JP1015760A patent/JPH0683831B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH02194894A (en) | 1990-08-01 |
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