JP3353091B2 - Water treatment device and water treatment facility using the same - Google Patents

Water treatment device and water treatment facility using the same

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Publication number
JP3353091B2
JP3353091B2 JP30167694A JP30167694A JP3353091B2 JP 3353091 B2 JP3353091 B2 JP 3353091B2 JP 30167694 A JP30167694 A JP 30167694A JP 30167694 A JP30167694 A JP 30167694A JP 3353091 B2 JP3353091 B2 JP 3353091B2
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JP
Japan
Prior art keywords
water
treated
tank
flow
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
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JP30167694A
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Japanese (ja)
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JPH07222975A (en
Inventor
哲夫 西田
Original Assignee
哲夫 西田
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Priority to JP30167694A priority Critical patent/JP3353091B2/en
Publication of JPH07222975A publication Critical patent/JPH07222975A/en
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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

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  • Activated Sludge Processes (AREA)
  • Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
  • Physical Water Treatments (AREA)

Description

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

【0001】[0001]

【産業上の利用分野】本発明は水処理装置に関し、更に
詳しくは、処理槽内の被処理水中に、強制的に、回転
流、縦渦等の大きな水流を生じさせて、或いはこれらに
加えて更に乱流及び渦糸、ヒルの球形渦、渦輪、カルマ
ン渦或いはテーラー渦等との如き小さな渦流れを発生さ
せることによって、被処理水に存在している油分や浮遊
物を集積除去する為の水処理装置、或いは及び被処理水
中に存在する微生物による生物学的水処理を、簡易且つ
確実に効率よく行うことが出来る水処理装置に関する。
えば、上記本発明の水処理装置は、雨水排水のポンプ
場、雨水と汚水を同一管渠に流す合流式下水道のポンプ
場、及び下排水処理施設等で、水質環境保全施設として
有効に用いられる。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a water treatment apparatus, and more particularly, to a method in which a large water flow such as a rotary flow or a vertical vortex is forcibly generated in water to be treated in a treatment tank, or in addition to these. In addition, turbulence and small vortices such as vortex, hill vortex, vortex ring, Karman vortex or Taylor vortex are generated to collect and remove oil and suspended matter present in the water to be treated. The present invention relates to a water treatment apparatus, and a water treatment apparatus that can easily, reliably, and efficiently perform biological water treatment using microorganisms present in water to be treated.
For example, the water treatment apparatus of the present invention, pumping stations rainwater, flowing rain water and sewage to the same sewer combined sewer pumping stations, and under wastewater treatment facilities, effectively used as a water conservation facility Can be

【0002】[0002]

【従来の技術】一般に、河川や湖沼の水、或いは産業排
水や生活排水等には、油等の浮遊物や砂等の固形物等、
種々雑多な夾雑物が含まれている。地球規模での環境保
護が叫ばれている今日、これらの水の浄化処理は、省エ
ネルギーで集約的に効率よく、且つ完全に行われること
が求められている。水の浄化処理の方法としては、物理
的処理方法を始め、化学的処理方法や生物学的処理方法
等がある。いずれの場合にも、被処理水中に含まれてい
る油分等の浮遊物や砂等の固形物は、水の浄化処理に直
接的に又は間接的に支障をもたらす為、事前に極力除去
しておくことが望ましい。
2. Description of the Related Art In general, water in rivers and lakes, or industrial wastewater or domestic wastewater, includes suspended matter such as oil and solid matter such as sand.
Various miscellaneous impurities are included. Nowadays, environmental protection on a global scale is called for, and it is required that these water purification treatments be performed intensively, efficiently, and completely with energy saving. Examples of the water purification method include a physical treatment method, a chemical treatment method, a biological treatment method, and the like. In any case, suspended matter such as oil and solid matter such as sand contained in the water to be treated directly or indirectly impede the water purification treatment. It is desirable to keep.

【0003】従来より、被処理水中に含まれている砂等
の固形物を除去する場合には一般に沈砂池や沈殿池が用
いられる。一方、浮遊物を除去する場合には一般にスク
リーン等が用いられている。しかし、上記固形物の除去
に沈殿池等を使用する場合には、広大な用地や、沈殿物
を取り除く為の高価で複雑な機構を有する装置が必要で
あるという問題がある。又、スクリーンを使用して微細
な浮遊固形物までも除去しようとする場合には、細かい
メッシュの高価なスクリーンを要するという問題や、浮
遊固形物によるスクリーンの目詰りの問題がある。
Conventionally, a sand basin or a sedimentation basin is generally used to remove solids such as sand contained in the water to be treated. On the other hand, when removing suspended matter, a screen or the like is generally used. However, when a sedimentation basin or the like is used for removing the solid matter, there is a problem that a vast site and an apparatus having an expensive and complicated mechanism for removing the sediment are required. Further, in the case of using a screen to remove even fine suspended solids, there is a problem that an expensive screen having a fine mesh is required and a problem of clogging of the screen due to the suspended solids.

【0004】上記従来技術に対し、本発明者は、特願平
1−85738号明細書等で、水処理施設における沈砂
池や、油分・浮遊物を除去する為の処理槽の略中央に水
平に回転する円筒を垂直に設けておき、該回転円筒を回
転させて被処理水に生じる水理的特性をうまく活用する
ことにより、固液分離の効率が良好で、安価で取扱いの
容易な固液分離装置を既に提案している。該装置では、
上記の回転円筒を油分や固形物等が含まれている被処理
水中で回転させて、油分や固形物をより迅速に且つ確実
に水から分離させる。そして、この装置は、回転円筒を
使用しない従来の方法に比べて、実際にかなり効率的に
油分等の浮遊物の分離や砂等の固形物等の分離がなされ
るが、設置場所における条件によっては浮遊物の分離が
未だ十分ではない。又、上記装置は、処理槽内の水位変
動に必ずしも十分には対応し得ないものであった。
[0004] In contrast to the above prior art, the present inventor disclosed in Japanese Patent Application No. 1-85738 and the like a horizontal settling tank in a water treatment facility or a substantially central processing tank for removing oil and suspended matter. A rotating cylinder is provided vertically, and the rotating cylinder is rotated to make good use of the hydraulic characteristics generated in the water to be treated, so that the solid-liquid separation efficiency is good, and the solid-liquid separation is inexpensive and easy to handle. A liquid separation device has already been proposed. In the device,
The rotary cylinder is rotated in the water to be treated containing oil and solids, so that the oil and solids can be separated from water more quickly and reliably. And, compared to the conventional method that does not use a rotating cylinder, this device actually separates suspended matters such as oil and solids such as sand, etc. quite efficiently, but depending on the conditions at the installation place. The separation of suspended matter is not yet sufficient. Further, the above-mentioned apparatus cannot always sufficiently cope with fluctuations in the water level in the treatment tank.

【0005】又、微生物による生物学的な排水処理(水
処理)方法は、二次汚染を引き起こしかねない化学的処
理方法と異なり、地球に優しい水処理方法として広く実
施されている。例えば、生物学的水処理方法の代表であ
る活性汚泥法の場合には、生物学的処理の効率化及び迅
速化を図る為に、被処理水を曝気して好気的な雰囲気中
で排水処理が行われている。又、酸化溝方式において
は、曝気の代わりに回転ドラムを用いて長い水路中に被
処理水を流し、流れて行く間に水面から被処理水中に酸
素を吸収させている。即ち、これらの従来方法のいずれ
においても、排水中における微生物の活動を活発化させ
る為の手段としては、被処理水中に酸素をいかに多く送
り込むことが出来るかを問題とするのみであって、これ
以外のより有力な微生物の活性化方法は見い出されてい
ないのが現状であり、排水の処理効率の向上には限界が
あった。
[0005] The biological wastewater treatment (water treatment) method using microorganisms is widely practiced as an earth-friendly water treatment method, unlike the chemical treatment method that may cause secondary pollution. For example, in the case of the activated sludge method, which is a representative of the biological water treatment method, in order to increase the efficiency and speed of the biological treatment, the treated water is aerated and drained in an aerobic atmosphere. Processing is taking place. Further, in the oxidation groove method, the water to be treated flows through a long water channel using a rotating drum instead of aeration, and oxygen is absorbed into the water to be treated from the water surface while flowing. That is, in any of these conventional methods, the only means for activating the activity of microorganisms in the wastewater is how much oxygen can be sent into the water to be treated. At present, no more effective method for activating microorganisms has been found, and there is a limit in improving the efficiency of wastewater treatment.

【0006】[0006]

【発明が解決しようとしている課題】従って本発明の目
的は、被処理水中に含有されている油分等の浮遊物や砂
等の固形物等を、処理槽内の被処理水の水位が一定、或
いは変動する場合のいずれにおいても、迅速に且つ確実
に分離除去し得る水処理装置を提供することにある。更
に本発明の目的は、処理槽内で絶え間なく流動している
被処理水中に、急流や緩流の状態を強制的に作ることに
よって、処理槽内に微生物の活き易い環境を実現し、微
生物に酸素を与え、運動をさせ、休憩させて、元気にさ
せて生物学的処理効率が向上する簡易且つ経済的な水処
理装置を提供することにある。
SUMMARY OF THE INVENTION Accordingly, an object of the present invention is to reduce the level of water to be treated in a treatment tank by removing suspended matter such as oil and solid matter such as sand contained in the treated water. Another object of the present invention is to provide a water treatment apparatus that can quickly and surely separate and remove any fluctuations. Furthermore, an object of the present invention is to realize an environment where microorganisms can easily be activated in the treatment tank by forcibly creating a rapid or slow flow state in the water to be treated that is constantly flowing in the treatment tank. It is an object of the present invention to provide a simple and economical water treatment apparatus that provides oxygen to a person, exercises, takes a break, and restores energy to improve biological treatment efficiency.

【0007】[0007]

【問題点を解決するための手段】上記目的は以下の本発
明によって達成される。即ち、本発明は、被処理水の流
入口と流出口とを有する処理槽と、処理槽内の被処理水
に強制的に一次流と一次流に付随する二次流とを発生さ
せる回転筒体とからなり、回転筒体の回転作用によって
被処理水を処理するようにした水処理装置であって、回
転筒体の外周に上下動自在の浮型輪を設けたものである
水処理装置、および、被処理水の流入口と流出口とを有
する処理槽と、処理槽内の被処理水に強制的に一次流と
一次流に付随する二次流とを発生させる回転筒体とから
なり、回転筒体の回転作用によって被処理水を処理する
ようにした水処理装置であって、処理槽の平面形状が円
形、楕円形、多角形及び長水路型のいずれかであり、且
つ処理槽内の偏心位置に回転筒体を設けたものである水
処理装置である。
The above object is achieved by the present invention described below. That is, the present invention provides a treatment tank having an inlet and an outlet for treated water, and a rotary cylinder for forcibly generating a primary flow and a secondary flow accompanying the primary flow in the treated water in the treatment tank. A water treatment apparatus comprising a body and configured to treat the water to be treated by a rotating action of a rotary cylinder, wherein a water ring is provided on the outer periphery of the rotation cylinder with a vertically movable floating ring. And a treatment tank having an inlet and an outlet for the water to be treated, and a rotary cylinder for forcibly generating a primary flow and a secondary flow accompanying the primary flow in the water to be treated in the treatment tank. A water treatment apparatus configured to treat the water to be treated by a rotating action of a rotary cylinder, wherein a planar shape of a treatment tank is any one of a circular shape, an elliptical shape, a polygonal shape, and a long channel type, and This is a water treatment apparatus in which a rotating cylinder is provided at an eccentric position in a tank.

【0008】[0008]

【作用】処理槽内において、回転筒体の回転作用によっ
て被処理水に一次流と二次流とを生じさせることによっ
て、被処理水中の油分等の浮遊物や砂等の固形物等を迅
速且つ確実に分離することが出来る。又、水処理装置に
おいて、一次流とこれに付随して生じる二次流の流路中
に適当な遮流体(流れに乱れを与えるものの総称)を設
けることによって、乱流や、所謂、渦糸、ヒルの球形
渦、渦輪、カルマン渦或いはテーラー渦等の如き小さな
渦流を無数に発生させることにより、微生物に回転運動
を与え、且つこれらの小さな渦流によって生じる緩流域
中において、被処理水中に存在している微生物を休息さ
せることにより、微生物が活性化して良質の分泌物を出
し、被処理水に対する生物学的処理効率を更に向上させ
ることが出来る。
[Function] In the treatment tank, a primary flow and a secondary flow are generated in the water to be treated by the rotating action of the rotary cylinder, so that floating substances such as oil and solid matter such as sand in the water to be treated can be quickly removed. And it can be separated reliably. In the water treatment apparatus, a turbulent flow or a so-called vortex is provided by providing an appropriate blocking fluid (general term for a turbulent flow) in a flow path of a primary flow and a secondary flow accompanying the primary flow. By generating countless small eddies such as spherical vortices, vortex rings, Karman vortices, or Taylor vortices, the microorganisms are given a rotational motion, and are present in the water to be treated in a gentle flow region created by these small eddies. By resting the microorganisms that have been treated, the microorganisms are activated to produce good-quality secretions, and the biological treatment efficiency for the water to be treated can be further improved.

【0010】上記本発明の装置において生物学的浄化処
理効率が向上する理由は明確ではないが、次の如く推測
している。即ち、被処理水中に存在している多くの微生
物は、べん毛やせん毛による運動能力を有し、絶えず運
動する習性を有している。この微生物の運動を助ける意
味において、本発明の水処理装置では、槽内に一次流及
び二次流に加えて大小の渦が絶えず無数に発生してお
り、緩流状態となる流域においては微生物が休息し、そ
の後は一層活発に活動することが出来る環境が被処理水
中に形成される為と考えられる。
The reason why the efficiency of the biological purification treatment in the apparatus of the present invention is improved is not clear, but it is speculated as follows. That is, many microorganisms existing in the water to be treated have a motor ability by flagella or hairs and have a habit of constantly exercising. In the sense of assisting the movement of the microorganisms, in the water treatment apparatus of the present invention, in addition to the primary flow and the secondary flow, countless large and small vortices are constantly generated in the tank. It is thought that the environment where the mosquitoes were resting and after which they could work more actively was formed in the treated water.

【0011】[0011]

【実施例】次に図面に示す好ましい実施例を参照して本
発明を更に詳しく説明する。本発明の水処理装置は、図
1(a)に示す様に、被処理水7の流入口1と流出口2
とを有する処理槽3と、該処理槽3内の被処理水7に強
制的に一次流4aと該一次流に付随する二次流4bとを
発生させる回転筒体5とからなることを特徴とする。
BRIEF DESCRIPTION OF THE DRAWINGS The invention will now be described in more detail with reference to a preferred embodiment shown in the drawings. As shown in FIG. 1 (a), the water treatment apparatus of the present invention has an inflow port 1 and an outflow port 2 for water 7 to be treated.
And a rotary cylinder 5 for forcibly generating a primary flow 4a and a secondary flow 4b accompanying the primary flow in the water 7 to be treated in the processing tank 3. And

【0012】本発明においては、例えば、図1(a)に
示す様に、処理槽3の被処理水7中に、上径、中径及び
下径の少なくとも一つが異なる形状の回転筒体5を設置
し、該筒体5を、処理槽3に取り付けらたモーター等に
よる駆動源(不図示)によって水平回転させることによ
って、処理槽3内に回転流である一次流4aと、該一次
流に付随して生じる二次流4bである縦渦とを発生させ
る。例えば、図1(a)に示した回転筒体5の場合、該
筒体5を水平回転させると、径の異ならない「ずんど
う」の円筒形状の筒体を回転させた場合よりも、大きな
回転流である一次流が発生する。そして、その強い回転
流による遠心力で被処理水が槽壁に打ちつけられ、この
部分の水位が高められ、強い二次流4bが発生する。
In the present invention, for example, as shown in FIG. 1 (a), a rotating cylinder 5 having at least one of an upper diameter, a middle diameter, and a lower diameter in a water 7 to be treated in a treatment tank 3. Is installed, and the cylinder 5 is horizontally rotated by a driving source (not shown) by a motor or the like attached to the processing tank 3, so that the primary flow 4 a, which is a rotational flow, and the primary flow And a vertical vortex, which is a secondary flow 4b, which is generated as a result. For example, in the case of the rotating cylinder 5 shown in FIG. 1A, when the cylinder 5 is horizontally rotated, a larger rotation is obtained than when a "square" cylindrical body having no different diameter is rotated. A primary flow is generated. Then, the water to be treated is hit against the tank wall by the centrifugal force of the strong rotating flow, the water level in this portion is raised, and a strong secondary flow 4b is generated.

【0013】本発明を特徴づける回転筒体5は、被処理
水中で緩急自在に回転可能であればいずれのものでもよ
いが、上記の図1(a)に示した形状の他、種々の外観
形態のものが挙げられる。例えば、図1(a)及び図2
(a)に示した様に、その径が連続的に変化している筒
体や、図2(b)に示した様に、上径、中径及び下径が
不連続的に変化している筒体等、いずれの形状の筒体も
好ましく使用される。その他、本発明に使用し得る回転
筒体5の外観形態の例を図6に示したが、この様な種々
の形状のものを使用することにより、図示した様な様々
な縦渦である二次流4bを強く発生させることによっ
て、被処理水の表面層に浮上した油分や浮遊物等を、回
転筒体内上部近傍、或いは処理槽の側壁近傍に集積させ
ることが出来る。
The rotary cylinder 5 which characterizes the present invention may be any one as long as it can rotate freely and slowly in the water to be treated. In addition to the shape shown in FIG. Form. For example, FIG. 1 (a) and FIG.
As shown in FIG. 2A, a cylindrical body whose diameter continuously changes, or as shown in FIG. 2B, whose upper, middle and lower diameters change discontinuously. A cylindrical body of any shape, such as a cylindrical body, is preferably used. In addition, FIG. 6 shows an example of the appearance of the rotary cylinder 5 which can be used in the present invention. By using such various shapes, various vertical vortices as shown in FIG. By strongly generating the next flow 4b, oils and suspended matters floating on the surface layer of the water to be treated can be accumulated near the upper part of the rotating cylinder or near the side wall of the treatment tank.

【0014】例えば、回転筒体5が、図1(a)に示し
た如き上径が大きい筒体である場合には、筒体5の回転
により生じる被処理水の流動により、比重の大きい砂等
の固形物10は槽底の中央部に集まり、一方、被処理水
表面にある比重の小さい油分等の浮遊物は強い2次流の
表面流により、処理槽3の側壁方向へと押し流される。
そこで、槽底の中央部に集積した砂等の固形物10は、
サンドポンプ等で、系外へと取り出され、処理される。
For example, when the rotating cylinder 5 is a cylinder having a large upper diameter as shown in FIG. 1A, the flow of the water to be treated generated by the rotation of the cylinder 5 causes the sand having a large specific gravity to flow. Solids 10 such as oil collect at the center of the bottom of the tank, while suspended matter such as oil having a low specific gravity on the surface of the water to be treated is swept toward the side wall of the treatment tank 3 by a strong secondary surface flow. .
Therefore, solids 10 such as sand accumulated at the center of the tank bottom are:
It is taken out of the system and processed by a sand pump or the like.

【0015】一方、油分等の浮遊物は、下記に述べる様
に溢流させた後、所定の処分がされる。上径の大きい筒
体5を用いる場合には、図1(a)に示す様に、処理槽
3の外側に続けて浮遊物ピット11を設け、更に、該ピ
ット11と処理槽3との区画壁に、上下動する構造のゲ
ート12を設けるのが好ましい。この様にすると、処理
槽3内の水位の違いに応じてゲート12を最適な位置に
置くことが出来、更に、ゲート12を水面位置から下に
下げることによって、油分や浮遊物等を多量に含む上部
の除去されるべき水(以下、「除去水」と略す)を処理
槽3内から容易に溢流させることが出来る。この結果、
除去水は、浮遊物ピット11内に導かれ、その後ポンプ
P等で系外に取り出される。
On the other hand, floating substances such as oil are overflowed as described below, and then disposed of. In the case of using the cylinder 5 having a large upper diameter, as shown in FIG. 1A, a suspended matter pit 11 is provided continuously outside the processing tank 3, and further, a partition between the pit 11 and the processing tank 3 is formed. It is preferable to provide a gate 12 that moves up and down on the wall. In this manner, the gate 12 can be placed at an optimal position according to the difference in water level in the treatment tank 3, and furthermore, by lowering the gate 12 from the water surface position, a large amount of oil and suspended matter can be obtained. The water to be removed at the upper portion (hereinafter, abbreviated as “removed water”) can easily overflow from the inside of the processing tank 3. As a result,
The removed water is guided into the suspended matter pit 11 and then taken out of the system by the pump P or the like.

【0016】この際、図1に示す本発明の水処理装置に
おいて、図1(b)及び(c)に示す様に、処理槽3壁
の内側に、被処理水7の表面に浮かぶ一対の浮子13、
13を連結する為の連結棒14、及び該連結棒14に固
定された複数の遮流体6を設けておくのが好ましい。こ
の結果、遮流体6の近くで小さな渦15が発生し、該遮
流体6に油分等の浮遊物が容易に引寄せられ、油分等の
浮遊物をより完全に且つ容易に被処理水表面中からピッ
ト11内へと移行させることが出来る。
At this time, in the water treatment apparatus of the present invention shown in FIG. 1, as shown in FIGS. 1 (b) and 1 (c) , a pair of floating members on the surface of the water 7 are provided inside the wall of the treatment tank 3. Float 13,
It is preferable to provide a connecting rod 14 for connecting the connecting members 13 and a plurality of fluid-blocking fluids 6 fixed to the connecting rod 14. As a result, a small vortex 15 is generated near the fluid shield 6, and the suspended matter such as oil is easily attracted to the fluid shield 6, and the suspended matter such as oil is more completely and easily removed from the surface of the water to be treated. From the pit 11.

【0017】処理槽3内の被処理水の水位が逐次変動す
る場合に、油分や浮遊物等を多量に含む除去水を集めて
分離するには、図3に示した様に、筒体上部が他の部分
よりも小径で、且つ側璧にスリット状の貫通孔16を設
けた回転筒体5を用い、処理槽3の中央部に除去水が集
まる様に、水処理装置を構成するのが好ましい。貫通孔
16の形状としては、所期の目的を達成し得るものであ
れば、図3に示した縦長のスリット状に限定されず、筒
体5の側壁の上下に複数設けられた横長のスリット状の
もの等いずれでよい。又、この場合に、筒体5内に溜っ
た除去水を上部ポンプPで吸引する方法としては、水位
に伴い上下動可能で、且つ水面に対し上向きの吸入口を
有する吸引装置で、除去水のみを吸引し取り出すのが好
ましい。
When the level of the water to be treated in the treatment tank 3 fluctuates sequentially, to collect and separate the removed water containing a large amount of oil and suspended matter, as shown in FIG. The water treatment apparatus is configured such that the diameter is smaller than that of the other parts, and the rotary cylinder 5 provided with the slit-shaped through-holes 16 in the side wall and the removed water is collected at the center of the treatment tank 3. Is preferred. The shape of the through-hole 16 is not limited to the vertically long slit shape shown in FIG. 3 as long as the intended purpose can be achieved, and a plurality of horizontally long slits provided above and below the side wall of the cylindrical body 5 are provided. Any shape may be used. In this case, as a method of sucking the removed water accumulated in the cylindrical body 5 by the upper pump P, the removed water can be moved up and down in accordance with the water level, and a suction device having a suction port facing upward with respect to the water surface can be used. It is preferable to suck and remove only.

【0018】又、本発明の装置においては、図4に示し
た様に、径が一定の回転筒体の外周に、処理槽3内の水
位の変動により筒体5の側壁を上下動する浮型輪17を
設けることによって、浮型輪17を含む筒体5の全体の
径の一部を拡大させることも出来る。この様にすれば、
例えば、図4(a)に点線で示した様に、浮型輪16
は、常に処理槽3内の被処理水表面上に位置し、且つそ
の状態で回転筒体5と共に回転する。この結果、被処理
水に水位変動が生じた場合でも、処理槽3内の下部側の
被処理水に生じる回転流よりも上部側の被処理水に生じ
る回転流の方が常に大きくなる。この為、先に説明した
と同様に、浮型輪17が設けられた回転筒体5を使用し
た場合にも、強い一次流及びこれに付随した強い二次流
が発生し、油分等を多量に含む除去水を被処理水から確
実に分離して浮遊物ピット11内に移行させて、取り出
すことが出来る。尚、浮型輪17の平面形状は、図4
(b)に示した様な外周円形状でもよいし、外周楕円形
状でもよい(不図示)。又、本発明で使用する上記の態
様の回転筒体としては、図4に示す様に、上下可能な
浮型輪17を回転円筒の外周に設けるのが好ましい。
又、本発明で使用する浮型輪付の回転円筒を、効率は低
下するが費用の安価な構造である棒状のものを回転円筒
に代えたものでもよい。
Further, in the apparatus of the present invention, as shown in FIG. 4, a floating cylinder which moves up and down on the side wall of the cylinder 5 due to the fluctuation of the water level in the treatment tank 3 is provided on the outer periphery of the rotating cylinder having a constant diameter. By providing the mold wheel 17, a part of the entire diameter of the cylindrical body 5 including the floating wheel 17 can be enlarged. If you do this,
For example, as shown by a dotted line in FIG.
Is always positioned on the surface of the water to be treated in the treatment tank 3 and rotates together with the rotary cylinder 5 in that state. As a result, even when the water level varies in the water to be treated, the rotational flow generated in the water to be treated on the upper side is always larger than the rotational flow generated in the water to be treated on the lower side in the treatment tank 3. Therefore, as described above, even when the rotary cylinder 5 provided with the floating wheel 17 is used, a strong primary flow and a strong secondary flow accompanying the primary flow are generated, and a large amount of oil and the like is generated. Can be reliably separated from the water to be treated, transferred to the suspended matter pit 11, and taken out. The plan shape of the floating wheel 17 is shown in FIG.
The outer peripheral circle shape as shown in (b) or the outer peripheral elliptical shape may be used (not shown). As the rotating cylinder of the above embodiments for use in the present invention, as shown in FIG. 4, preferably provided with vertical movement possible浮型wheel 17 on the outer periphery of the rotating cylinder.
In addition, the rotating cylinder with a floating ring used in the present invention has low efficiency.
A rotating cylinder is a rod-shaped structure
May be used instead of.

【0019】本発明の水処理装置は、処理槽3内に、先
に述べた各種形状の回転筒体5が設置されて構成される
が、回転筒体5は、例えば、図4に示した様に、従来と
同様に処理槽3の略中央位置に設置してもよいし、図5
に示した様に、槽内の偏心位置に設置してもよい。偏心
位置に設置した場合には、槽内の略中央部に設置した場
合とは異なり、一次流である回転流4aが変則的なもの
となり、一次流4aに付随して生じる処理槽3内の二次
流である縦渦(不図示)も変則的なものとなる。この結
果、処理槽3内に一次流と、これにより引き起こされる
二次流のみならず、その他の複雑な乱流や渦流が発生
し、処理水中に淀みが出来る結果、油分等を多量に含む
除去水の浮遊物濃度が高くなる場合があり好ましい。こ
の為、処理槽の平面形状も円形のみにこだわることな
く、図5に示した様に、楕円形であっても、その他、多
角形及び長水路型等であってもよい。
The water treatment apparatus of the present invention is configured by installing the above-described rotary cylinders 5 of various shapes in the treatment tank 3, and the rotary cylinder 5 is, for example, shown in FIG. 5 may be installed at substantially the center of the processing tank 3 as in the conventional case.
As shown in the above, it may be installed at an eccentric position in the tank. When installed at the eccentric position, unlike the case where it is installed at a substantially central portion in the tank, the rotating flow 4a which is the primary flow becomes irregular, and the inside of the processing tank 3 which accompanies the primary flow 4a is generated. Vertical vortices (not shown), which are secondary flows, are also irregular. As a result, not only the primary flow and the secondary flow caused by this, but also other complicated turbulences and eddies are generated in the processing tank 3, and stagnation is generated in the processing water, thereby removing a large amount of oil and the like. This is preferable because the concentration of suspended solids in water may increase. For this reason, the planar shape of the treatment tank is not limited to a circular shape, but may be an elliptical shape as shown in FIG. 5, or may be a polygonal shape or a long channel type.

【0020】処理槽3の別の好ましい例としては、例え
ば、被処理水から分離される物の比重が大である場合に
は、流入口1を水深方向の中位に設け、一方、分離され
る物の比重が小さい場合は流入口1を水深方向の浅い位
置に設ける。又、被処理水の流入方向は、処理槽3内の
被処理水の流れの乱れを最小限にする様に、処理槽3の
円周の接線方向に設け、処理槽3に流入した被処理水が
処理槽3の壁面に沿って流れ易い構造とすることが好ま
しい。処理槽3の構成材料、容量等としては、被処理水
の条件、即ち、処理場所、水量、含まれている油分や固
形物等の種類や量等によって適当に変更すればよく、例
えば、処理槽3はコンクリート、鋼板、銅板等の金属、
硬質塩化ビニル樹脂等のプラスチック、木材、遠赤セラ
ミック等、任意の材質で形成され、且つ、通常は0.5
〜500m3 の容積を有し得るがこれに限定されない。
尚、被処理水を処理し、被処理水を処理槽3から次の処
理工程へと移行させる場合には、上記した回転筒体5を
偏心位置に設置した方が処理施設全体でスペース的に好
ましい場合が多い。
As another preferred example of the treatment tank 3, for example, when the specific gravity of the substance separated from the water to be treated is large, the inlet 1 is provided at a middle position in the water depth, When the specific gravity of the object is small, the inlet 1 is provided at a shallow position in the water depth direction. The flow direction of the water to be treated is set in the tangential direction of the circumference of the processing tank 3 so as to minimize the disturbance of the flow of the water to be treated in the processing tank 3. It is preferable that the structure is such that water easily flows along the wall surface of the processing tank 3. The constituent material, volume, etc. of the treatment tank 3 may be appropriately changed depending on the conditions of the water to be treated, that is, the treatment place, the amount of water, and the type and amount of oils and solids contained therein. Tank 3 is made of metal such as concrete, steel plate, copper plate, etc.
It is made of any material such as plastic such as hard vinyl chloride resin, wood, far-red ceramic, etc., and is usually 0.5
It may have a volume of to 500m 3 is not limited thereto.
When the water to be treated is treated and the water to be treated is transferred from the treatment tank 3 to the next treatment step, it is better to install the rotary cylinder 5 at an eccentric position in terms of space in the entire treatment facility. Often preferred.

【0021】又、本発明の水処理装置に使用される回転
筒体5を回転させる手段としては、例えば、回転筒体5
を槽3内に垂直に位置させた場合に、筒体5の上端外周
に歯車等を備えることによって外周駆動する方法でも、
或いは他に支障がなければ中心軸を有する筒体5を使用
し、該中心軸を自由回転可能に支持体から懸垂する方法
でもよい。以上の如き回転筒体5は、処理槽3の直径の
10〜30%程度の直径を有しており、その長さは処理
槽3の大きさや深さ等によって、又、要求される処理能
力と動力費との関係で任意に変更することが出来、又、
場合によっては、処理槽3内に平列又は直列に2個以上
の回転筒体を併設することも出来る。尚、回転筒体5
は、強度、防腐性等を考慮するとステンレス鋼等の防蝕
性の材料、電磁波を発生する材料、銅の様な抗菌材料等
で形成することが好ましい。
Means for rotating the rotary cylinder 5 used in the water treatment apparatus of the present invention includes, for example, the rotary cylinder 5
In the method of driving the outer periphery by providing a gear or the like on the outer periphery of the upper end of the cylindrical body 5 when the
Alternatively, if there is no other problem, a method may be used in which a cylindrical body 5 having a central axis is used and the central axis is suspended from the support so as to be freely rotatable. The rotary cylinder 5 as described above has a diameter of about 10 to 30% of the diameter of the processing tank 3, and its length depends on the size and depth of the processing tank 3 and the required processing capacity. And can be changed arbitrarily in relation to the power cost,
In some cases, two or more rotating cylinders may be provided in the processing tank 3 in parallel or in series. The rotating cylinder 5
In consideration of strength, antiseptic properties, and the like, it is preferable that the material be formed of a corrosion-resistant material such as stainless steel, a material that generates electromagnetic waves, an antibacterial material such as copper, or the like.

【0022】以上述べた様に、本発明の水処理装置によ
れば、被処理水中の砂等の比重の大なる夾雑物が槽底
に、そして、油分やその他の比重の小さい浮遊物は被処
理水の上層に容易に分離される結果、処理済水中に含ま
れる油等の浮遊物や砂等の固形物が極力軽減された状態
となるので、例えば、本発明の装置を排水処理場におけ
る前処理に用い、その後に各種浄化処理を行うことによ
って、排水処理場における浄化処理の効率が従来に比べ
格段に向上する。又、本発明の水処理装置は、排水の活
性汚泥処理の処理槽や、薬品処理(化学処理)の反応槽
として用いるか、これらの処理設備の前処理槽として使
用するのが極めて好ましい。即ち、本発明の水処理装置
を、昨今問題とされることの多い公共用水域の水質保全
の為に、一般的な雨水の排水ポンプ場や、雨水と汚水を
同一管渠で流す合流式下水道のポンプ場等で使用すれ
ば、公共水域に放流する水質を向上させることが出来
る。
As described above, according to the water treatment apparatus of the present invention, impurities having a large specific gravity such as sand in the water to be treated are deposited on the bottom of the tank, and oil and other suspended matters having a small specific gravity are deposited on the tank bottom. As a result of being easily separated into the upper layer of the treated water, the suspended matter such as oil and solid matter such as sand contained in the treated water are in a state where the solid matter is reduced as much as possible. By using it for the pretreatment and performing various purification treatments thereafter, the efficiency of the purification treatment at the wastewater treatment plant is significantly improved as compared with the conventional case. Further, the water treatment apparatus of the present invention is very preferably used as a treatment tank for activated sludge treatment of wastewater, a reaction tank for chemical treatment (chemical treatment), or as a pretreatment tank for these treatment facilities. That is, the water treatment apparatus of the present invention is used for general rainwater drainage pumping stations and a combined sewerage system in which rainwater and sewage flow through the same conduit for the purpose of preserving the water quality of public water bodies that are often regarded as a problem these days. If used at a pumping station, the quality of water discharged into public waters can be improved.

【0023】次に、生物学的水処理効率が格段に向上す
る本発明の水処理装置について説明する。この装置は、
被処理水の流入口と流出口とを有する処理槽と、処理槽
内の被処理水に強制的に一次流と一次流に付随する二次
流とを発生させる回転筒体とからなり、回転筒体の回転
作用によって被処理水を処理するようにした水処理装置
であって、更に好ましくは一次流の流路および/または
二次流の流路に少なくとも1個の遮流体を設けたもので
ある。この装置においては、遮流体によって水流中に小
さな渦流れを連続、間欠若しくは緩急自在に生じさせ、
これらの流れの変化によって適量の酸素を被処理水中に
吸収させて、処理槽内の微生物に運動と休息を与えて活
性化し、微生物に良質の分泌物を出させることができ
る。即ち、上記で説明したと同様の回転筒体5の回転に
よって生じる一次流および/または二次流の流路に、丸
棒、角棒、または孔あき板等の遮流体を設けることによ
り、被処理水中に、カルマン渦のような小さな渦流を現
出させたり、遮流体から離れて渦が消えた緩流の状態を
現出させたりすることができる。このような状態で、被
処理水中の微生物に、必要な酸素を連続的に、または間
欠的に与えながら、微生物を運動させたり休息させたり
して生物活動を活発化させ、より良質の処理済水を得る
ことを可能とする。
Next, a water treatment apparatus according to the present invention, in which the biological water treatment efficiency is remarkably improved, will be described. This device is
A treatment tank having an inlet and an outlet for the water to be treated, and a rotating cylinder for forcibly generating a primary flow and a secondary flow accompanying the primary flow in the water to be treated in the treatment tank, A water treatment apparatus configured to treat water to be treated by a rotating action of a cylindrical body, and more preferably provided with at least one fluid blocking fluid in a primary flow path and / or a secondary flow path. It is. In this device, a small vortex flow is continuously, intermittently, or slowly generated in a water flow by a shielding fluid,
By the change of these flows, an appropriate amount of oxygen is absorbed into the water to be treated, and the microorganisms in the treatment tank are activated by exercising and resting, so that the microorganisms can emit good-quality secretions. In other words, by providing a fluid block such as a round bar, a square bar, or a perforated plate in the flow path of the primary flow and / or the secondary flow generated by the rotation of the rotary cylinder 5 as described above, In the treated water, a small vortex like a Karman vortex can appear, or a slow flow state in which the vortex has disappeared away from the fluid blocking fluid can appear. In such a state, the required oxygen is continuously or intermittently supplied to the microorganisms in the water to be treated, and the microorganisms are exercised or rested to activate the biological activities, thereby improving the quality of the treated water. Make it possible to get water.

【0024】図7に示した例は、回転筒体5の外周表面
上に棒状物等からなる遮流体6を設け、更に、処理槽の
側壁面上に凹凸状の遮流体6を設けた例であり、これら
の遮流体6近傍には、図7(b)に示したように小さな
渦流15が発生する。また、図8(a)に示したよう
に、回転筒体5の外周近傍に、回転筒体5の外周面との
間に隙間ができるような固定した壁状の遮流体6を設け
るか、図8(b)に示したように、回転筒体5の内部に
円柱状の遮流体6を槽底に固定して設けると、回転筒体
5の内側とこれらの遮流体6の外面との間に狭い隙間が
形成され、この隙間に規則正しいテーラー渦15が生じ
る。
The example shown in FIG. 7 is an example in which a fluid barrier 6 made of a rod or the like is provided on the outer peripheral surface of the rotary cylinder 5 and furthermore, an uneven fluid barrier 6 is provided on the side wall surface of the processing tank. A small vortex 15 is generated near these fluid blocking fluids 6 as shown in FIG. In addition, as shown in FIG. 8A, a fixed wall-shaped fluid blocking member 6 is provided near the outer periphery of the rotating cylinder 5 so as to form a gap between the outer periphery of the rotating cylinder 5. As shown in FIG. 8 (b), when the cylindrical fluid-shielding fluid 6 is fixedly provided at the bottom of the tank inside the rotary cylinder 5, the inner surface of the rotary cylinder 5 and the outer surface of these fluid-shielding fluids 6 can be separated. Narrow gaps are formed between them, where regular Taylor vortices 15 are formed.

【0025】更に、図9に示した例は、処理槽3内の流
れの中に、丸棒、平板等の種々の形状の遮流体6を設け
た例である。遮流体6を設ける位置としては、例えば、
図9(a)及び(b)に示した様な槽壁面や、その他、
槽内における種々の位置に設けることが出来る。又、遮
流体6の形状としては、例えば、図9〜図11に示した
様な種々の形状が挙げられるが、これらの遮流体6を一
次流である回転流と二次流である縦渦の中に置くと、乱
流となったり、更には図10及び図11に示した様な規
則的な或いは不規則的な種々の渦流を生じる。ここで、
図12に、渦糸、ヒルの球形渦、渦輪、カルマン渦或い
はテーラー渦の典型的なものを示す。
Further, the example shown in FIG. 9 is an example in which various shapes of fluid shielding 6 such as a round bar and a flat plate are provided in the flow in the processing tank 3. As a position where the fluid blocking fluid 6 is provided, for example,
The tank wall as shown in FIGS. 9A and 9B, and others,
It can be provided at various positions in the tank. Examples of the shape of the shielding fluid 6 include various shapes such as those shown in FIGS. 9 to 11. , Turbulence and various regular or irregular vortices as shown in FIGS. 10 and 11 are generated. here,
FIG. 12 shows a typical example of a vortex, a spherical vortex of a hill, a vortex ring, a Karman vortex or a Taylor vortex.

【0026】本発明の水処理装置において、上記の様な
種々の形状の遮流体6が槽壁面や槽内或いは回転筒体5
に種々設けられている実施例では、処理槽3内では、大
きな流れの一次流である回転流と二次流である縦渦に加
え、例えば、図11で示したカルマン渦列等の細かい渦
流れがこれらの大きな流れの中に生じ、槽内の被処理水
全体に渡って種類及び強度の異なる流れが絶え間なく生
じる。この結果、被処理水表面からの酸素の吸収或いは
槽底からの散気によって必要な酸素が処理槽3内に行き
渡ると同時に、処理槽3内では、渦流によって微生物に
活動的な回転渦運動等が与えられる。渦流が弱まり緩流
となっている領域では微生物がゆっくり休息する等、微
生物にとってより健康で元気になる住み易い環境が提供
される。この為、微生物がより活発に活動することが出
来るので、有機性排水の浄化作用を更に促進し得る。
In the water treatment apparatus of the present invention, the fluid shielding 6 having various shapes as described above is applied to the tank wall, the inside of the tank, or the rotating cylinder 5.
In the processing tank 3, in addition to the rotating flow as the primary flow of the large flow and the vertical vortex as the secondary flow, for example, a fine vortex such as the Karman vortex street shown in FIG. Flows occur in these large streams, and streams of different types and intensities occur continuously throughout the water to be treated in the tank. As a result, necessary oxygen is distributed into the treatment tank 3 by absorbing oxygen from the surface of the water to be treated or diffusing from the bottom of the tank. Is given. In a region where the eddy current is weakened and the current is gentle, the living environment is provided that is more healthy and vibrant for the microorganisms, such as the microorganisms resting slowly. For this reason, microorganisms can be more active, and the action of purifying organic wastewater can be further promoted.

【0027】従来、排水の生物学的な浄化処理法の一種
として、酸化溝方式(オキシデーションディッチ法)が
ある。かかる方法は、活性汚泥長時間曝気法の一種であ
り、循環水路にエアレーターを設置して排水を循環させ
ながら、エアレーションを行い排水を浄化する方式であ
り、通常、横軸型、縦軸型、ドラフトチューブ型等があ
る。例えば、図13に示す様に、長水路型(ドーナツ
形)の溝からなる処理槽中で、攪拌機の一種である水平
位置に設置した回転ドラム5を回し、排水等の被処理水
を循環水路内で回流させながら被処理水表面から酸素を
吸収させる方法がある。
Conventionally, there is an oxidation ditch method (oxidation ditch method) as one type of biological purification treatment of wastewater. Such a method is a type of activated sludge long-time aeration method, and is a method of purifying wastewater by aeration while installing an aerator in a circulation channel and circulating wastewater. And a draft tube type. For example, as shown in FIG. 13, a rotating drum 5 installed at a horizontal position, which is a kind of a stirrer, is rotated in a treatment tank having a long channel (doughnut type) groove to circulate water to be treated such as drainage. There is a method in which oxygen is absorbed from the surface of the water to be treated while being circulated inside.

【0028】この様な酸化溝方式に、本発明を応用する
場合には、回転ドラム5の形状は、従来から使用されて
いる一般的な円筒形状のものでも勿論よいが、図1、図
2及び図6に示す様な、上径、中径及び下径の少なくと
も一つが異なる回転筒体5を使用するのが好ましい。図
13に示した例について説明すると、本例では、上記し
た様な回転筒体5を、これまで説明してきた処理槽3内
に垂直に設置した例とは異なり、回転筒体5を水平に設
置する。この結果、図13に示す様に、鼓型の回転筒体
5を回転した場合には、筒体5の径が大きい循環水路の
壁面近傍で強い一次流が生じ、循環水路の中央部ではこ
れと比べ弱い一次流が発生する。又、これらの一次流の
強い方から弱い方へ二次流が生ずる為、循環水路内では
通常の循環流とは異なる縦渦や水平渦等の複雑の渦流が
発生する。
When the present invention is applied to such an oxidation groove method, the shape of the rotating drum 5 may be of a general cylindrical shape which has been conventionally used, but FIGS. It is preferable to use a rotating cylinder 5 having at least one of an upper diameter, a middle diameter, and a lower diameter as shown in FIG. The example shown in FIG. 13 will be described. In this example, unlike the example in which the rotary cylinder 5 as described above is vertically installed in the processing tank 3 described above, the rotary cylinder 5 is horizontally set. Install. As a result, as shown in FIG. 13, when the drum-shaped rotary cylinder 5 is rotated, a strong primary flow is generated near the wall surface of the circulation channel where the diameter of the cylinder 5 is large. A weaker primary flow is generated. In addition, since secondary flows are generated from the stronger primary flow to the weaker primary flow, complicated vortices such as vertical vortices and horizontal vortices different from normal circulating flows are generated in the circulation channel.

【0029】又、図14に示した例では、先に説明した
様に、循環水路に垂直に回転筒体5を設置する。この場
合は、図7〜図9に示した例で説明した様に、回転筒体
5を水平方向に回転させることによって、一次流である
水平方向の回転流と、これに付随して二次流である縦渦
が発生する。この場合も、上記と同様に、循環水路内に
は循環流があるので、図7〜図9に示した例の場合より
も複雑な渦流等を生じる。本発明の装置では、更に、こ
れらの流れの中に各種の形状の遮流体6が設けられてい
る為、先に述べたと同様、カルマン渦等の各種の小さな
渦流れが更に発生する。尚、遮流体6は、図13及び図
14に示した様に、例えば、回転筒体の表面、槽内の側
壁や底面等、循環水路内の一次流の流路及び二次流の流
路のいずれかに設ければよい。
In the example shown in FIG. 14, the rotary cylinder 5 is installed vertically in the circulation channel as described above. In this case, as described in the examples shown in FIGS. 7 to 9, by rotating the rotary cylinder 5 in the horizontal direction, the horizontal rotation flow as the primary flow and the secondary rotation A vertical vortex is generated as a flow. Also in this case, as in the above case, since there is a circulating flow in the circulating water channel, a more complicated vortex and the like than in the examples shown in FIGS. In the apparatus of the present invention, since various shapes of the fluid blocking fluid 6 are provided in these flows, various small vortex flows such as Karman vortices are generated as described above. As shown in FIGS. 13 and 14, for example, the primary fluid flow path and the secondary flow flow path in the circulating water channel, such as the surface of the rotary cylinder, the side wall and the bottom surface in the tank, as shown in FIGS. May be provided in any of the above.

【0030】本発明を応用した上記の酸化溝方式による
生物学的な水処理装置においては、循環水路内や回転筒
体5に設ける遮流体6の位置及び形状を適宜に設計する
ことにより、更に好ましくは、上記設計した装置を間欠
運転等することによって、自然界の河川におけると同様
な、急流、せせらぎ、たまり等の様々な水の流れを再現
することが出来る。即ち、被処理水中の微生物の生物活
動を、自然界におけると同様にすることが出来る。その
結果、本発明を応用した酸化溝方式による水処理装置に
おいては、表面からの被処理水中への酸素溶解効果に加
え、種々の流れの中に遮流体を置くことにより、微生物
に回転渦運動等が与えられたり、渦流の消えた緩流では
微生物にゆっくりと休息が与えられ、処理領域が微生物
にとって住み易い環境となる。
In the biological water treatment apparatus according to the above-described oxidation groove system to which the present invention is applied, the position and shape of the fluid blocking member 6 provided in the circulating water channel and the rotary cylinder 5 are appropriately designed to further improve the performance. Preferably, by intermittently operating the above-designed device, it is possible to reproduce various flows of water, such as rapids, babbling, and pools, as in a river in nature. That is, the biological activity of the microorganisms in the water to be treated can be made the same as in the natural world. As a result, in the water treatment device of the oxidation ditch method to which the present invention is applied, in addition to the effect of dissolving oxygen from the surface into the water to be treated, by placing a fluid barrier in various flows, the microorganisms can be swirled. In the slow flow where the eddy current disappears, the microorganisms are slowly relieved, and the treatment area becomes an environment where the microorganisms can easily live.

【0031】以上の様に、本発明を活性汚泥法等の生物
学的方法に用いる水処理装置の処理槽は、固液分離に使
用する装置の場合と同様に、図7〜図9に示す様な、自
然流若しくは不図示のポンプ等で強制的に送られてくる
処理対象の被処理水の流入口1と、処理済の水を排出す
る排水口2を有し、更に被処理水中に酸素を強制的に溶
存させる為に空気を送る散気手段とを有するものが好ま
しい。又、適当な容量の槽である限りその形状は円柱
形、矩形、楕円柱形等特に限定されない。例えば、図1
3及び図14で示した様に、酸化溝方式による生物学的
な浄化処理法に使用する場合には、長い溝を有する長水
路型(ドーナツ形)の処理槽を使用する。
As described above, the treatment tank of the water treatment apparatus using the present invention for the biological method such as the activated sludge method is shown in FIGS. 7 to 9 as in the case of the apparatus used for solid-liquid separation. It has an inlet 1 for the water to be treated, which is forcibly sent by a natural flow or a pump or the like (not shown), and a drain 2 for discharging the treated water. It is preferable to have an air blowing means for sending air to forcibly dissolve oxygen. The shape of the tank is not particularly limited as long as the tank has an appropriate capacity, such as a cylinder, a rectangle, and an ellipse. For example, FIG.
As shown in FIG. 3 and FIG. 14, when used in a biological purification treatment method using an oxidized groove method, a long water channel type (doughnut type) treatment tank having a long groove is used.

【0032】[0032]

【発明の効果】以上説明した様に、本発明によれば、処
理槽内に生じる一次流と、それに付随して生じる二次流
との働きにより、油分等の浮遊物を多量に含む除去水と
砂等の固形物等を容易に且つ迅速に分離することが出来
る。更に、遮流体を設け、これにより発生する小さな渦
流によって、分離効率をより向上させることが出来る。
又、本発明によれば、処理槽内を、自然流に近い、急
流、せせらぎ及び溜りといった様々な流れが生じた住み
易い環境とすることが出来る為、微生物がより元気に活
動して、微生物による浄化作用が著しく進行して水の生
物学的な浄化処理効率を著しく向上させることが出来
る。
As described above, according to the present invention, the removal of water containing a large amount of suspended matter such as oil is performed by the action of the primary stream generated in the treatment tank and the secondary stream generated accompanying the primary stream. And solids such as sand can be easily and quickly separated. Further, a shielding fluid is provided, and the small vortex generated thereby can further improve the separation efficiency.
Further, according to the present invention, the inside of the treatment tank can be made a livable environment in which various flows such as a natural flow, a rapid flow, a babbling and a pool have occurred, so that the microorganisms can be more active and the microorganisms can be activated. The purification action of the water significantly progresses, and the biological purification efficiency of water can be significantly improved.

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

【図1】本発明の水処理装置を固液分離に用いた場合の
概略図である。
FIG. 1 is a schematic diagram when the water treatment apparatus of the present invention is used for solid-liquid separation.

【図2】本発明の水処理装置を固液分離に用いた場合の
概略図である。
FIG. 2 is a schematic diagram when the water treatment apparatus of the present invention is used for solid-liquid separation.

【図3】本発明の水処理装置を固液分離に用いた場合の
概略図である。
FIG. 3 is a schematic diagram when the water treatment apparatus of the present invention is used for solid-liquid separation.

【図4】本発明の水処理装置を固液分離に用いた場合の
概略図である。
FIG. 4 is a schematic diagram when the water treatment apparatus of the present invention is used for solid-liquid separation.

【図5】本発明の水処理装置を使用した水処理施設の一
例の概略平面図である。
FIG. 5 is a schematic plan view of an example of a water treatment facility using the water treatment device of the present invention.

【図6】本発明の水処理装置を構成する回転筒体の例の
概略断面図である。
FIG. 6 is a schematic sectional view of an example of a rotary cylinder constituting the water treatment apparatus of the present invention.

【図7】本発明の水処理装置を生物学的処理に用いた場
合の概略図である。
FIG. 7 is a schematic diagram when the water treatment apparatus of the present invention is used for biological treatment.

【図8】本発明の水処理装置を生物学的処理に用いた場
合の概略図である。
FIG. 8 is a schematic diagram when the water treatment apparatus of the present invention is used for biological treatment.

【図9】本発明の水処理装置を生物学的処理に用いた場
合の概略図である。
FIG. 9 is a schematic diagram when the water treatment apparatus of the present invention is used for biological treatment.

【図10】本発明の水処理装置で使用される遮流体とそ
れにより発生する渦を示す概略図である。
FIG. 10 is a schematic diagram showing a fluid barrier used in the water treatment apparatus of the present invention and vortices generated thereby.

【図11】本発明の水処理装置で使用される遮流体とそ
れにより発生する渦を示す概略図である。
FIG. 11 is a schematic diagram showing a fluid barrier used in the water treatment apparatus of the present invention and vortices generated thereby.

【図12】渦流の種類を示す概略図ある。FIG. 12 is a schematic diagram showing types of eddies.

【図13】本発明の水処理装置を酸化溝方式の生物学的
処理に用いた場合の概略図である。
FIG. 13 is a schematic diagram of a case where the water treatment apparatus of the present invention is used for biological treatment using an oxidation ditch method.

【図14】本発明の水処理装置を酸化溝方式の生物学的
処理に用いた場合の別の例の概略図である。
FIG. 14 is a schematic view of another example when the water treatment apparatus of the present invention is used for biological treatment using an oxidation ditch method.

【符号の説明】[Explanation of symbols]

1:固液混合物の流入口 2:固形物等の排出口 5:回転筒体 10:処理槽 1: Inlet for solid-liquid mixture 2: Outlet for solids, etc. 5: Rotating cylinder 10: Processing tank

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 被処理水の流入口と流出口とを有する処
理槽と、処理槽内の被処理水に強制的に一次流と一次流
に付随する二次流とを発生させる回転筒体とからなり、
回転筒体の回転作用によって被処理水を処理するように
した水処理装置であって、回転筒体の外周に上下動自在
の浮型輪を設けたものである水処理装置。
1. A processing tank having an inlet and an outlet for water to be treated, and a rotary cylinder for forcibly generating a primary flow and a secondary flow accompanying the primary flow in the water to be treated in the processing tank. Consisting of
What is claimed is: 1. A water treatment apparatus comprising: a water treatment apparatus configured to treat water to be treated by a rotating action of a rotating cylinder, wherein a floating wheel that can move up and down is provided on an outer periphery of the rotation cylinder.
【請求項2】 被処理水の流入口と流出口とを有する処
理槽と、処理槽内の被処理水に強制的に一次流と一次流
に付随する二次流とを発生させる回転筒体とからなり、
回転筒体の回転作用によって被処理水を処理するように
した水処理装置であって、処理槽の平面形状が円形、楕
円形、多角形及び長水路型のいずれかであり、且つ処理
槽内の偏心位置に回転筒体を設けたものである水処理装
置。
2. A processing tank having an inlet and an outlet for water to be treated, and a rotary cylinder for forcibly generating a primary flow and a secondary flow accompanying the primary flow in the water to be treated in the processing tank. Consisting of
A water treatment apparatus configured to treat water to be treated by a rotating action of a rotary cylinder, wherein a plan shape of a treatment tank is any of a circle, an ellipse, a polygon, and a long channel, and A water treatment apparatus comprising a rotary cylinder provided at an eccentric position of the water treatment apparatus.
JP30167694A 1993-12-16 1994-11-11 Water treatment device and water treatment facility using the same Expired - Fee Related JP3353091B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP30167694A JP3353091B2 (en) 1993-12-16 1994-11-11 Water treatment device and water treatment facility using the same

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP34270993 1993-12-16
JP5-342709 1993-12-16
JP30167694A JP3353091B2 (en) 1993-12-16 1994-11-11 Water treatment device and water treatment facility using the same

Publications (2)

Publication Number Publication Date
JPH07222975A JPH07222975A (en) 1995-08-22
JP3353091B2 true JP3353091B2 (en) 2002-12-03

Family

ID=26562816

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP3353091B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1338571A1 (en) * 2001-11-14 2003-08-27 OMS Verwaltungs- und Beteiligungs GmbH Waste water treatment unit
JP4765022B2 (en) * 2005-03-25 2011-09-07 株式会社西原環境 Solid-liquid separator

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