JPH11253982A - Method and apparatus for treating waste water - Google Patents

Method and apparatus for treating waste water

Info

Publication number
JPH11253982A
JPH11253982A JP10055522A JP5552298A JPH11253982A JP H11253982 A JPH11253982 A JP H11253982A JP 10055522 A JP10055522 A JP 10055522A JP 5552298 A JP5552298 A JP 5552298A JP H11253982 A JPH11253982 A JP H11253982A
Authority
JP
Japan
Prior art keywords
carrier
aeration
aeration tank
tank
air diffusion
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.)
Withdrawn
Application number
JP10055522A
Other languages
Japanese (ja)
Inventor
Kei Baba
圭 馬場
Toshiaki Tsubone
俊明 局
Tatsuo Takechi
辰夫 武智
Shinichi Endo
伸一 遠藤
Yukihiko Okamoto
幸彦 岡本
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.)
JFE Engineering Corp
Original Assignee
NKK Corp
Nippon Kokan Ltd
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 NKK Corp, Nippon Kokan Ltd filed Critical NKK Corp
Priority to JP10055522A priority Critical patent/JPH11253982A/en
Priority to CA 2303020 priority patent/CA2303020A1/en
Priority to EP98961546A priority patent/EP1033348A4/en
Priority to PCT/JP1998/005893 priority patent/WO1999044950A1/en
Priority to US09/508,410 priority patent/US6497819B1/en
Publication of JPH11253982A publication Critical patent/JPH11253982A/en
Withdrawn legal-status Critical Current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

  • Biological Treatment Of Waste Water (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a waste water treatment apparatus capable of preventing the sedimentation of a carrier the lower part of the air diffusion device arranged in a reaction tank or to the lower part of the air diffusion device of an aeration tank and an apparatus therefor. SOLUTION: Air diffusing devices 3 are arranged to an aeration tank 1 receiving a carrier 2 growing bacteria to biologically treat waste water or to aeration sub-units connected by partition walls containing screens capable of separating the carrier 2, and an underwater stirrer 5 generating water streams in the parts under the air diffusion devices 3 is arranged and the carrier 2 under the air diffusion devices 3 is fluidized by the water streams from the underwater stirrer 5 to be prevented from sedimentation under the air diffusion devices 3. In the waste treatment apparatus thus constituted, the sedimentation of the carrier 2 under the air diffusion devices 3 is eliminated and the treatment efficiency as the aeration tank is kept and the treatment capacity corresponding to a plan value can be obtained.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、廃水処理方法およ
びその装置に関し、詳しくは廃水中の有機物、無機物を
生物学的に浄化処理するに当たって、廃水の浄化作用を
営む微生物を有機高分子物質または無機物質を主成分と
する粒子状の担体に包括固定化もしくは付着固定化もし
くは結合固定化した微生物固定化担体を使用する廃水処
理方法およびその装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and an apparatus for treating wastewater, and more particularly to biologically purifying organic and inorganic substances in wastewater. The present invention relates to a wastewater treatment method and a device using a microorganism-immobilized carrier immobilized, attached, or bonded and immobilized on a particulate carrier mainly composed of an inorganic substance.

【0002】[0002]

【従来の技術】周知のように、廃水処理装置には、標準
活性汚泥法における反応槽と微生物固定化担体を投入し
た反応槽等がある。微生物固定化担体を投入した反応槽
では、標準活性汚泥法における反応槽と比較して、微生
物濃度を高濃度に保持することが可能であり、廃水中の
有機物、無機物を分解する処理効率を高めるとことがで
きる利点を有している。微生物による分解を促進させる
ための酸素供給を行う散気装置を反応槽に設置したもの
を曝気槽と称される。
2. Description of the Related Art As is well known, a wastewater treatment apparatus includes a reaction tank in a standard activated sludge method and a reaction tank charged with a microorganism-immobilized carrier. In a reaction tank containing a microorganism-immobilized carrier, it is possible to maintain a high concentration of microorganisms compared to a reaction tank in the standard activated sludge method, and to increase the treatment efficiency of decomposing organic and inorganic substances in wastewater. It has the advantage that it can be. A device provided with a diffuser for supplying oxygen for promoting decomposition by microorganisms in a reaction tank is called an aeration tank.

【0003】図4は、微生物固定化担体を用いた廃水処
理装置の概略図を示し、同図(a)はその平面図であ
り、同図(b)はそのX−Y線に沿った断面図である。
同図の廃水処理装置は、微生物固定化担体2が投入され
た水深5m程度の曝気槽1に、槽下部全面から散気を行
う散気管3aに接続した散気装置3が備えられた全面散
気方式の曝気槽で形成されている。通常、全面散気方式
の散気装置3は、槽底面より200mmから600mm
上方に設置されている。そして、散気装置3は、槽底面
からの空気の吹き出しによる撹拌効果が低いために、担
体2の流動に必要な水流速が十分に得られず、担体2
は、槽底部に堆積物6として沈積する傾向にある。
FIG. 4 is a schematic view of a wastewater treatment apparatus using a microorganism-immobilized carrier. FIG. 4A is a plan view of the apparatus, and FIG. 4B is a sectional view taken along the line XY. FIG.
The wastewater treatment apparatus shown in FIG. 1 includes an aeration tank 1 having a depth of about 5 m into which a microorganism-immobilized carrier 2 is charged, and a diffuser 3 connected to a diffuser pipe 3a for diffusing air from the bottom of the tank. It is formed with a pneumatic aeration tank. Normally, the diffuser 3 of the full-surface diffusion method is 200 mm to 600 mm from the bottom of the tank.
It is installed above. In addition, the air diffuser 3 has a low stirring effect due to the blowing of air from the bottom of the tank, so that the water flow rate required for the flow of the carrier 2 cannot be sufficiently obtained.
Tend to deposit as deposits 6 on the bottom of the tank.

【0004】このような曝気槽1の散気装置3の下部に
担体2の沈積が発生することは、曝気槽1におけるデッ
ドスペースの生成と処理に寄与する担体量の減少を招く
結果となり、水処理設備の処理能力を低下させることに
なる。このような散気装置3の下部における担体沈積を
防止するため、従来は、散気装置3の下部の空間をウレ
タン樹脂等で満たす方法が行われたり、沈積する担体量
に相当する量の担体を補充して処理能力の低下を防止す
る方法が採られている。
[0004] Such deposition of the carrier 2 in the lower portion of the aeration device 3 of the aeration tank 1 results in the generation of dead space in the aeration tank 1 and a decrease in the amount of the carrier contributing to the treatment. This will reduce the processing capacity of the processing equipment. Conventionally, in order to prevent such carrier deposition in the lower part of the air diffuser 3, a method of filling the space below the air diffuser 3 with urethane resin or the like is performed, or a carrier having an amount corresponding to the amount of the carrier to be deposited is used. In order to prevent a decrease in processing capacity.

【0005】[0005]

【発明が解決しようとする課題】従来の曝気槽では、散
気装置下部への担体の沈積を防止する方法として、散気
装置の下部の空間をウレタン樹脂等で満たす方法がなさ
れており、ウレタン樹脂等の充填工事を行うための材料
費および人件費が必要となる問題がある。また、ウレタ
ン樹脂等が充填された散気装置の下部領域は、デッドス
ペースとなるために、予めこのデッドスペースを考慮し
て大きな反応槽を建設することによって、反応槽として
必要な容積を確保しなければならず、建設費が大になる
という問題がある。
In the conventional aeration tank, as a method for preventing the deposition of the carrier on the lower portion of the air diffuser, a method of filling the space below the air diffuser with urethane resin or the like has been used. There is a problem that a material cost and a labor cost for performing the filling work of the resin or the like are required. In addition, since the lower region of the air diffuser filled with urethane resin or the like becomes a dead space, a large reaction tank is constructed in advance in consideration of the dead space to secure a necessary volume as a reaction tank. And the construction cost increases.

【0006】さらに、従来の曝気槽では、散気装置の下
部に沈積した担体量を補充して処理能力の低下を防止し
ており、このような方法では、必要担体量の増加に伴っ
て担体費用が大となるという問題がある。また、散気装
置の下部に沈積した担体の占める容積がデッドスペース
となって実質的な反応槽の容積が減少して、処理水質の
悪化を招くという問題と、沈積した担体同士の間に形成
される空間に汚泥が堆積し腐敗して処理水質の悪化を招
くという問題がある。
Further, in the conventional aeration tank, the amount of the carrier deposited in the lower part of the aeration device is replenished to prevent a reduction in the processing capacity. In such a method, the amount of the carrier is increased as the required amount of the carrier increases. There is a problem that the cost becomes large. In addition, the volume occupied by the carrier deposited in the lower part of the aeration device becomes a dead space, and the actual volume of the reaction tank is reduced, resulting in deterioration of the treatment water quality. There is a problem that sludge accumulates and decomposes in the space to be treated, resulting in deterioration of treated water quality.

【0007】本発明は、上記のような課題を解決するた
めになされたものであり、反応槽に設置した散気装置あ
るいは曝気槽の散気装置の下部への微生物固定化担体の
沈積を防止し得る廃水処理方法およびその装置を提供す
るものである。
SUMMARY OF THE INVENTION The present invention has been made to solve the above-mentioned problems, and prevents deposition of a microorganism-immobilized carrier on the lower part of an aeration device installed in a reaction tank or an aeration tank. The present invention provides a wastewater treatment method and a device therefor.

【0008】[0008]

【課題を解決するための手段】本発明は、上記課題に鑑
みなされたものであり、請求項1の発明は、微生物を育
成する担体を投入して生物学的に廃水処理を行う曝気槽
もしくは前記担体の分離可能なスクリーンを含む仕切壁
で連結した曝気槽サブユニットに酸素供給用の散気装置
が配置され、前記散気装置より下部に配置された水中撹
拌機によって水流を発生させて担体を流動させ、前記散
気装置の下部に担体が沈積するのを防止することを特徴
とする廃水処理方法である。この構成によれば、水中撹
拌機による水流によって、散気装置の下部の担体を流動
させて、散気装置下部の水中撹拌機における担体の沈積
が解消され、反応槽としての処理効率が維持され、かつ
設計値通りの処理能力を得ることができる。
Means for Solving the Problems The present invention has been made in view of the above problems, and the invention of claim 1 is directed to an aeration tank or a tank for biologically treating wastewater by adding a carrier for growing microorganisms. An aeration device for supplying oxygen is disposed in an aeration tank subunit connected by a partition wall including a separable screen of the carrier, and a water flow is generated by an underwater agitator disposed below the aeration device. The wastewater treatment method is characterized in that the carrier is caused to flow to prevent the carrier from depositing in the lower part of the air diffuser. According to this configuration, the carrier at the lower part of the diffuser is caused to flow by the water flow of the underwater stirrer, and the deposition of the carrier in the underwater stirrer at the lower part of the diffuser is eliminated, and the processing efficiency as a reaction tank is maintained. , And a processing capacity as designed.

【0009】また、請求項2の発明は、微生物を育成す
る担体を投入して生物学的に廃水処理を行う曝気槽もし
くは前記担体の分離可能なスクリーンを含む仕切壁で連
結した曝気槽サブユニットと、前記曝気槽と曝気サブユ
ニットに配置された酸素供給用の散気装置と、前記散気
装置の下部に配置された水中撹拌機とを具備することを
特徴とする廃水処理装置である。この構成によれば、水
中撹拌機による水流によって、散気装置の下部の担体を
流動させて、散気装置下部の水中撹拌機における担体に
沈積が解消され、反応槽としての処理効率が維持され、
かつデッドスペースが発生することなく、設計値通りの
処理能力を得ることができる装置である。
[0009] The invention of claim 2 provides an aeration tank for introducing a carrier for growing microorganisms and biologically treating wastewater or an aeration tank subunit connected by a partition wall including a separable screen for the carrier. A wastewater treatment apparatus, comprising: an aeration device for supplying oxygen arranged in the aeration tank and the aeration subunit; and a submersible agitator arranged below the aeration device. According to this configuration, the carrier in the lower part of the air diffuser is caused to flow by the water flow by the underwater agitator, and the deposition on the carrier in the underwater agitator below the air diffuser is eliminated, and the processing efficiency as a reaction tank is maintained. ,
In addition, it is an apparatus capable of obtaining a processing capacity as designed without generating dead space.

【0010】また、請求項3の発明は、前記水中撹拌機
は、槽底部に2mから20mの間隔で設置したことを特
徴とする請求項2に記載の廃水処理装置である。この構
成によれば、散気装置下部の全面に水流を発生させるこ
とができるので、担体を無駄なく浮遊させて槽全体に分
散させることができるので、廃水中の有機高分子物質を
分解する処理能力を維持し得る働きを有する。
The invention according to claim 3 is the wastewater treatment apparatus according to claim 2, wherein the underwater stirrer is installed at an interval of 2 m to 20 m at the bottom of the tank. According to this configuration, since a water flow can be generated over the entire lower surface of the air diffuser, the carrier can be floated without waste and dispersed throughout the tank. Has the ability to maintain the ability.

【0011】[0011]

【発明の実施の形態】以下、本発明の廃水処理方法およ
びその装置の実施の形態について、図面を参照して説明
する。図1は、本発明の廃水処理装置の一実施形態を示
す概略図である。同図(a)はその平面図であり、同図
(b)はそのX−Y線に沿った断面図である。同図にお
いて、廃水処理装置は、微生物固定化担体2が投入され
る曝気槽1と、曝気槽1の底部全面に空気が送り込まれ
る散気管3aで接続された酸素供給用散気装置3と、散
気装置3の下部であって、曝気槽1の底部のほぼ中央に
設置された水中撹拌機5とで構成されている。微生物固
定化担体2は、有機高分子物質または無機物質を主成分
とする粒子状の物質であり、微生物を包括固定化もしく
は結合固定化するものである。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments of a wastewater treatment method and apparatus according to the present invention will be described below with reference to the drawings. FIG. 1 is a schematic diagram showing an embodiment of the wastewater treatment device of the present invention. FIG. 1A is a plan view thereof, and FIG. 1B is a cross-sectional view thereof along the line XY. In FIG. 1, a wastewater treatment apparatus includes an aeration tank 1 into which a microorganism-immobilized carrier 2 is charged, an oxygen supply air diffusion apparatus 3 connected by an air diffusion pipe 3a through which air is supplied to the entire bottom of the aeration tank 1, A lower part of the air diffuser 3 and an underwater stirrer 5 installed substantially at the center of the bottom of the aeration tank 1. The microorganism-immobilized carrier 2 is a particulate substance mainly composed of an organic polymer substance or an inorganic substance, and is used for immobilizing or binding and immobilizing microorganisms.

【0012】図2は、本発明の廃水処理装置の他の実施
形態を示す概略図である。同図(a)はその平面図であ
り、同図(b)はそのX−Y線に沿った断面図である。
同図の廃水処理装置は、曝気槽1がサブユニット1a,
1bで構成されている。サブユニット1a,1bの境界
部の曝気槽流出部は、担体2と被処理水とを分離するた
めに担体分離用スクリーンを含む仕切壁4が設置され、
サブユニット1aは曝気槽サブユニットである。そし
て、散気装置3と水中撹拌機5とは、図1と同一条件で
配置されている。
FIG. 2 is a schematic diagram showing another embodiment of the wastewater treatment apparatus of the present invention. FIG. 1A is a plan view thereof, and FIG. 1B is a cross-sectional view thereof along the line XY.
In the wastewater treatment apparatus shown in the figure, the aeration tank 1 has a subunit 1a,
1b. A partition wall 4 including a carrier separation screen is installed at the outflow portion of the aeration tank at the boundary between the subunits 1a and 1b to separate the carrier 2 and the water to be treated.
Subunit 1a is an aeration tank subunit. The air diffuser 3 and the underwater stirrer 5 are arranged under the same conditions as in FIG.

【0013】これら実施形態の廃水処理装置は、曝気槽
1もしくは担体の分離可能なスクリーンを含む仕切壁4
で連結している曝気槽サブユニット1aの底部全面に散
気装置3が設置された全面散気方法の曝気槽であり、散
気装置3から空気が送り込まれて、槽内の被処理水に浮
遊分散する担体2に微生物を育生するのに適した環境に
維持されている。水中撹拌機5は、担体2を水流によっ
て、底部に沈積するのを阻止する働きを有する。水中撹
拌機5は、散気装置3の下部の槽底部より散気装置3の
下部に至る200mmから600mmの程度の深さの空
間に設置され、水中撹拌機5により、散気装置3の下部
の担体2の流動に十分な水流量を発生させて、散気装置
3の下部での担体2の沈積を防止する。
The wastewater treatment apparatus according to these embodiments includes an aeration tank 1 or a partition wall 4 including a separable screen of a carrier.
This is an aeration tank of the whole-surface aeration method in which the aeration device 3 is installed on the entire bottom surface of the aeration tank subunit 1a connected by the air. The air is sent from the aeration device 3 to the treated water in the tank. The environment suitable for growing microorganisms is maintained on the carrier 2 which is suspended and dispersed. The underwater stirrer 5 has a function of preventing the carrier 2 from being deposited on the bottom by the water flow. The underwater stirrer 5 is installed in a space having a depth of about 200 mm to 600 mm extending from the bottom of the tank below the air diffuser 3 to the lower part of the air diffuser 3. A sufficient water flow rate for the flow of the carrier 2 is generated to prevent deposition of the carrier 2 at the lower portion of the air diffuser 3.

【0014】水中撹拌機5は、散気装置3の底部で担体
2が十分流動するような水流速であることが必要であ
り、水中撹拌機5は、槽底面の担体2を含む被処理水を
吸い込み、上方に吹き上げて撹拌させる。また、逆に水
中撹拌機5の上方の被処理水を下方に吹き出して、散気
装置3の底部に十分な水流を与えて担体2の分散効果を
得るものである。
The underwater stirrer 5 needs to have a water flow rate such that the carrier 2 flows sufficiently at the bottom of the diffuser 3. , And blow up to stir. Conversely, the water to be treated above the underwater stirrer 5 is blown downward to give a sufficient water flow to the bottom of the diffuser 3 to obtain the dispersion effect of the carrier 2.

【0015】なお、担体2が投入された曝気槽1もしく
は担体2の分離可能なスクリーンを含む仕切壁4で連結
されている曝気槽サブユニット1aの長さおよび幅が2
mから20m以内ならば、図1,図2に示したように、
水中撹拌機5は、槽底部ほぼ中央に配置することによっ
て、充分な水流を発生させることができる。
The length and width of the aeration tank 1 into which the carrier 2 is charged or the length and width of the aeration tank subunit 1a connected by a partition wall 4 including a separable screen of the carrier 2 are set to 2.
If it is within 20m from m, as shown in FIGS. 1 and 2,
The underwater stirrer 5 can generate a sufficient water flow by being arranged at substantially the center of the tank bottom.

【0016】また、曝気槽が長さおよび幅が2mから2
0m以上の比較的大きな容積を有する場合は、図3に示
したように、散気装置3の下部に設置する水中撹拌機5
の配置間隔Aは、2m〜20m間隔、好ましくは5m〜
10m間隔とする。このような間隔で配置することによ
って、槽底部全面の散気装置の下部において担体2を流
動させるために必要な水流速を得ることが可能となる。
なお、曝気槽の底面の面積に応じて、所定個数配置して
もよい。水中撹拌機5を所定の面積当たりに1個数を配
置してもよく、例えば水中撹拌機5を5m2 に1個の割
合で配置するようにしてもよい。
Further, the length and width of the aeration tank are from 2 m to 2 m.
In the case of having a relatively large volume of 0 m or more, as shown in FIG.
Is 2 m to 20 m, preferably 5 m to
The interval is 10 m. By arranging at such intervals, it becomes possible to obtain a water flow rate necessary for flowing the carrier 2 under the air diffuser on the entire bottom of the tank.
A predetermined number may be arranged according to the area of the bottom surface of the aeration tank. One underwater stirrer 5 may be arranged per predetermined area, for example, one underwater stirrer 5 may be arranged at a rate of 5 m 2 .

【0017】[0017]

【実施例】次に、本発明の一実施例と従来例とを比較し
て、その有効性について説明する。本実施例は、図2の
廃水処理装置の全面散気方式による曝気槽であり、槽底
部中央に、水中撹拌機5が配置されている。水中撹拌機
5によって、槽底部ほぼ全面に水流速を発生させること
により、担体2の沈積を防止するようにした。本実施例
の有効性については、本実施例と、従来例である図4に
示した水中撹拌機5を設置しない曝気装置とを比較実験
によって説明する。両者の廃水処理装置は、同一形状と
し、それぞれの曝気装置は、同一形状で水面積負荷10
m/日以下を満足する沈殿池を接続して取水した。沈殿
池から水処理装置に投入された汚水の水質は、表1に示
した。表2は、本実施例と従来例との処理結果を示して
おり、散気装置の下部における被処理水のx,y,z軸
3方向の水流速の平均値を示した。
Next, an embodiment of the present invention will be compared with a conventional example to explain its effectiveness. This embodiment is an aeration tank of the wastewater treatment apparatus of FIG. 2 using a full-surface aeration method, and an underwater stirrer 5 is disposed at the center of the bottom of the tank. The submerged stirrer 5 was used to generate a water flow velocity over almost the entire bottom of the tank, thereby preventing the deposition of the carrier 2. The effectiveness of the present embodiment will be described by a comparative experiment between the present embodiment and a conventional example of the aeration apparatus without the underwater stirrer 5 shown in FIG. Both wastewater treatment devices have the same shape, and each aeration device has the same shape and a water area load of 10%.
A sedimentation basin satisfying m / day or less was connected and water was taken. Table 1 shows the water quality of the sewage supplied from the sedimentation basin to the water treatment apparatus. Table 2 shows the processing results of the present embodiment and the conventional example, and shows the average values of the water velocities in the x, y, and z-axis three directions of the water to be treated in the lower part of the air diffuser.

【0018】[0018]

【表1】 [Table 1]

【0019】[0019]

【表2】 [Table 2]

【0020】その有効性は、表2から明らかである。本
実施例は、散気装置下部に水中撹拌機を設置することに
よって、廃水の良好な処理結果が得られることが実証さ
れた。比較例である気泡発生装置を設置しない場合、透
明塩化ビニール製の曝気槽の側面から観測した結果、槽
底部において担体と汚泥の混合物が散気装置下部全面に
沈積した。本実施例では、表2における散気装置下部の
平均水流速が増大して担体を十分に流動させることが可
能であることが分かった。
The effectiveness is clear from Table 2. In this example, it was proved that a good treatment result of the wastewater can be obtained by installing the underwater stirrer below the air diffuser. When the bubble generator as a comparative example was not installed, the mixture of the carrier and the sludge was deposited on the entire lower surface of the diffuser at the bottom of the tank as a result of observation from the side of the aeration tank made of transparent vinyl chloride. In the present example, it was found that the average water flow velocity in the lower part of the air diffuser in Table 2 was increased, and the carrier was able to flow sufficiently.

【0021】[0021]

【発明の効果】上記記述したように、本発明によれば、
微生物固定化担体を投入した曝気槽で廃水を処理するに
当たって、担体が投入された曝気槽もしくは曝気槽サブ
ユニットの酸素供給用散気装置より下部に水中撹拌機を
設置することにより、散気装置下部に水流を発生させる
ことができるとともに、このような単純かつ容易な方法
および装置によって、散気装置の下部での担体の沈積を
防止することができることから、廃水処理装置の建設費
が安価となる利点があり、既存の曝気槽や反応槽に簡単
に改良を加えることができる利点がある。
As described above, according to the present invention,
In treating wastewater in the aeration tank charged with the microorganism-immobilized carrier, the submerged stirrer is installed below the oxygen supply diffuser for the aeration tank or the aeration tank subunit in which the carrier is charged. A water flow can be generated in the lower part, and since such a simple and easy method and apparatus can prevent the deposition of the carrier in the lower part of the diffuser, the construction cost of the wastewater treatment apparatus can be reduced. There is an advantage that an existing aeration tank or reaction tank can be easily improved.

【0022】また、本発明によれば、担体を曝気槽内で
充分分散させることができるために、曝気槽容積および
投入した担体の全体を有効に利用することができる利点
があり、曝気槽として設計値通りの処理能力を得ること
ができるとともに、投入された担体を充分に浮遊分散さ
せて、廃水中の有機高分子物質等を担体に寄生する微生
物によって、廃水の安定した処理が可能となる効果を有
する利点がある。
Further, according to the present invention, since the carrier can be sufficiently dispersed in the aeration tank, there is an advantage that the volume of the aeration tank and the whole of the loaded carrier can be effectively used. It is possible to obtain the treatment capacity as designed, and to sufficiently disperse and disperse the loaded carrier, and to stably treat the wastewater by the microorganisms that parasitize the organic polymer substances and the like in the wastewater on the carrier. There is an advantage of having an effect.

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

【図1】(a)は本発明に係る廃水処理装置である曝気
槽の実施形態を示す平面図、(b)はそのX−Y線に沿
った断面図である。
FIG. 1A is a plan view showing an embodiment of an aeration tank as a wastewater treatment apparatus according to the present invention, and FIG. 1B is a cross-sectional view taken along the line XY.

【図2】(a)は本発明に係る廃水処理装置である曝気
槽サブユニットの実施形態を示す平面図、(b)はその
X−Y線に沿った断面図である。
FIG. 2A is a plan view showing an embodiment of an aeration tank subunit which is a wastewater treatment apparatus according to the present invention, and FIG. 2B is a cross-sectional view taken along line XY.

【図3】本発明に係る廃水処理装置の他1の実施形態を
示す断面図である。
FIG. 3 is a sectional view showing another embodiment of the wastewater treatment apparatus according to the present invention.

【図4】(a)は従来の廃水処理装置である曝気槽の一
例を示す平面図、(b)はそのX−Y線に沿った断面図
である。
FIG. 4A is a plan view showing an example of an aeration tank as a conventional wastewater treatment apparatus, and FIG. 4B is a cross-sectional view taken along the line XY.

【符号の説明】[Explanation of symbols]

1 曝気槽 2 微生物固定化担体 3 散気装置 4 仕切壁 5 水中撹拌機 Reference Signs List 1 aeration tank 2 carrier for immobilizing microorganisms 3 diffuser 4 partition wall 5 underwater stirrer

フロントページの続き (72)発明者 遠藤 伸一 東京都千代田区丸の内一丁目1番2号 日 本鋼管株式会社内 (72)発明者 岡本 幸彦 東京都千代田区丸の内一丁目1番2号 日 本鋼管株式会社内Continued on the front page (72) Inventor Shinichi Endo 1-2-1, Marunouchi, Chiyoda-ku, Tokyo Nihon Kokan Co., Ltd. (72) Inventor Yukihiko Okamoto 1-2-1, Marunouchi, Chiyoda-ku, Tokyo Nihon Kokan Stock In company

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 微生物を育成する担体を投入して生物学
的に廃水処理を行う曝気槽もしくは前記担体の分離可能
なスクリーンを含む仕切壁で連結した曝気槽サブユニッ
トに酸素供給用の散気装置が配置され、前記散気装置よ
り下部に配置された水中撹拌機によって水流を発生させ
て担体を流動させ、前記散気装置の下部に担体が沈積す
るのを防止することを特徴とする廃水処理方法。
Aeration for supplying oxygen to an aeration tank for introducing a carrier for growing microorganisms and biologically treating wastewater or an aeration tank subunit connected by a partition wall including a separable screen for the carrier. Wastewater characterized in that a device is arranged, a carrier is caused to flow by generating a water flow by an underwater stirrer arranged below the aeration device, and the carrier is prevented from being deposited at a lower portion of the aeration device. Processing method.
【請求項2】 微生物を育成する担体を投入して生物学
的に廃水処理を行う曝気槽もしくは前記担体の分離可能
なスクリーンを含む仕切壁で連結した曝気槽サブユニッ
トと、 前記曝気槽と曝気サブユニットに配置された酸素供給用
の散気装置と、 前記散気装置の下部に配置された水中撹拌機とを具備す
ることを特徴とする廃水処理装置。
2. An aeration tank for introducing a carrier for growing microorganisms and biologically treating wastewater, or an aeration tank subunit connected by a partition wall including a separable screen for the carrier, and the aeration tank and aeration. A wastewater treatment apparatus comprising: an oxygen supply air diffuser arranged in a subunit; and a submersible agitator arranged below the air diffuser.
【請求項3】 前記水中撹拌機は、槽底部に2mから2
0mの間隔で設置したことを特徴とする請求項2に記載
の廃水処理装置。
3. The underwater stirrer is provided at the bottom of the tank from 2 m to 2 m.
The wastewater treatment device according to claim 2, wherein the wastewater treatment device is installed at an interval of 0 m.
JP10055522A 1998-03-06 1998-03-06 Method and apparatus for treating waste water Withdrawn JPH11253982A (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
JP10055522A JPH11253982A (en) 1998-03-06 1998-03-06 Method and apparatus for treating waste water
CA 2303020 CA2303020A1 (en) 1998-03-06 1998-12-25 Method and apparatus for treating waste water
EP98961546A EP1033348A4 (en) 1998-03-06 1998-12-25 Method and apparatus for treating waste water
PCT/JP1998/005893 WO1999044950A1 (en) 1998-03-06 1998-12-25 Method and apparatus for treating waste water
US09/508,410 US6497819B1 (en) 1998-03-06 1998-12-25 Method and apparatus for treating waste water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10055522A JPH11253982A (en) 1998-03-06 1998-03-06 Method and apparatus for treating waste water

Publications (1)

Publication Number Publication Date
JPH11253982A true JPH11253982A (en) 1999-09-21

Family

ID=13001058

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10055522A Withdrawn JPH11253982A (en) 1998-03-06 1998-03-06 Method and apparatus for treating waste water

Country Status (1)

Country Link
JP (1) JPH11253982A (en)

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