JP2003200185A - Carrier flowing out prevention mechanism for water treatment device - Google Patents

Carrier flowing out prevention mechanism for water treatment device

Info

Publication number
JP2003200185A
JP2003200185A JP2001390401A JP2001390401A JP2003200185A JP 2003200185 A JP2003200185 A JP 2003200185A JP 2001390401 A JP2001390401 A JP 2001390401A JP 2001390401 A JP2001390401 A JP 2001390401A JP 2003200185 A JP2003200185 A JP 2003200185A
Authority
JP
Japan
Prior art keywords
carrier
water
tank
bed tank
filter bed
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP2001390401A
Other languages
Japanese (ja)
Other versions
JP3831661B2 (en
Inventor
Takeshi Yokomizo
武 横溝
Katsumi Kawashima
克美 川島
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.)
Sanki Engineering Co Ltd
Original Assignee
Sanki Engineering Co 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 Sanki Engineering Co Ltd filed Critical Sanki Engineering Co Ltd
Priority to JP2001390401A priority Critical patent/JP3831661B2/en
Publication of JP2003200185A publication Critical patent/JP2003200185A/en
Application granted granted Critical
Publication of JP3831661B2 publication Critical patent/JP3831661B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime 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

Abstract

<P>PROBLEM TO BE SOLVED: To provide a catchment mechanism for a moving bed type aerobic filtration bed capable of collecting good treated water by inhibiting flowing out of a solid substance to the treated water without inhibiting a flow of a carrier at the time of washing. <P>SOLUTION: Raw water is flowed from an upper part of an aerobic filtration bed tank 10 filled with a carrier and a fine solid substance in the raw water is captured by the carrier during that it descends in the filtration bed tank. After the contaminant dissolved in water is decomposed by microorganisms deposited on a surface of the carrier, the treated water flows out from a catchment area 12 at a lower part of the filtration bed tank to the outside of the tank. Whereas, after the carrier on which the solid substance is deposited by a biological treatment and which descends is raised by an air lift pipe 29 provided at a center of the filtration bed tank 10, the carrier from which the solid substance is separated is circulated into the filtration bed tank. In the filtration bed tank 10, a carrier flowing out prevention mechanism is disposed, which comprises a diffusion umbrella provided on an outer periphery of a protection pipe 25 of the air lift pipe for diffusing the carrier descending into the catchment area 12; a catchment cylinder 30 extending from a small diameter side of the diffusion umbrella to a height arriving at a half part of a central water collecting part 11 at the filtration bed tank; and a treated water flowing out pipe 14 projected from an upper outer wall of the water-collection cylinder to the outside of the tank. <P>COPYRIGHT: (C)2003,JPO

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、下降流式水処理装
置である移動床式好気性ろ床において、処理水質を悪化
させることなく、処理水を集水できる担体流出防止機構
に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a carrier outflow prevention mechanism capable of collecting treated water in a moving bed type aerobic filter which is a downflow type water treatment apparatus without deteriorating the quality of the treated water.

【0002】[0002]

【従来の技術】有機物によって汚染された水を微生物の
働きによって浄化する方法の1つとして、微生物を固体
粒子に付着させ、これを通過する原排水中の汚染物質と
接触させ、原排水を好気性消化し浄化する生物膜浄化装
置がある。この生物膜浄化装置の代表的なものとして、
下降流式水処理装置(好気性ろ床)が知られている。こ
の装置は、担体(濾材)を充填した好気性ろ床槽の下部
から空気を吹き込み、原水を上部から流入させ、ろ床槽
内を下降する間に原水中の微細な固形物を捕捉し、微生
物により分解したのち、ろ床槽下部の集水機構から処理
水を流出させると共に、生物処理によって固形物が付着
した担体を、ろ床槽の中央に設けたエアリフト管により
吸い込んで上部に上げ、固形物を分離した担体をろ床槽
内へ循環させるようにしたものである。
2. Description of the Related Art As one of the methods of purifying water polluted by organic substances by the action of microorganisms, the microorganisms are attached to solid particles and contacted with the pollutants in the raw wastewater passing through the solid particles so that the raw wastewater is preferably treated. There is a biofilm purifier that digests and purifies the air. As a representative of this biofilm purification device,
A downflow type water treatment device (aerobic filter) is known. This device blows air from the lower part of an aerobic filter bed tank filled with a carrier (filter medium), allows raw water to flow in from the upper part, and captures fine solid matter in the raw water while descending in the filter bed tank, After being decomposed by microorganisms, the treated water is caused to flow out from the water collecting mechanism at the bottom of the filter bed tank, and the carrier to which solid matter is attached by biological treatment is sucked up by the air lift pipe provided at the center of the filter bed tank and raised to the upper part, The carrier from which the solid matter is separated is circulated in the filter bed tank.

【0003】ろ槽には担体(例えばアンスラサイト、活
性炭、軽量骨材等で粒径2〜10mm程度のもの)が充填
され、ろ槽の下部には水処理室で生物処理された処理水
を集水する拡散傘が設けられている。水処理室には生物
処理に必要な空気を曝気ブロアによって原水中に吹き込
む散気装置が配置されている。原水は、水処理室内の担
体中を通過する際に、担体表面に付着した微生物の働き
により浄化される。原水中に含まれるSS成分及びBO
D成分等は生物処理により担体表面に付着し蓄積する。
このため、担体間に目詰まりが生じ原水の通過抵抗が増
大する。このように、担体に付着した固形物を除去する
必要から、洗浄が行なわれる。即ち、最下部の担体を、
エアリフト管を通して上部に上げ、分離装置により固形
物を分離する。一般に、良好な水質の処理水を得るため
には、ろ槽内において、処理時の水の流れを均一にし
て処理効率を上げること、洗浄時の担体の流れを妨げ
ずかつ緩やかなものとして、洗浄効率を上げ、処理水へ
の固形物の流出を抑えること、低流速で均一に集水し
て、処理水への固形物の流出および担体の流出を抑える
こと、が必要である。
The filter tank is filled with a carrier (for example, anthracite, activated carbon, lightweight aggregate, etc., having a particle size of about 2 to 10 mm), and the lower part of the filter tank is filled with treated water biologically treated in a water treatment chamber. There is a diffusion umbrella to collect water. The water treatment room is equipped with an air diffuser for blowing air necessary for biological treatment into raw water by an aeration blower. Raw water is purified by the action of microorganisms adhering to the surface of the carrier when passing through the carrier in the water treatment chamber. SS component and BO contained in raw water
The component D and the like adhere to and accumulate on the surface of the carrier by biological treatment.
For this reason, clogging occurs between the carriers and the passage resistance of the raw water increases. In this way, washing is performed because it is necessary to remove the solid matter attached to the carrier. That is, the bottom carrier,
It is raised to the upper part through an air lift pipe, and a solid material is separated by a separating device. Generally, in order to obtain treated water of good water quality, in the filter tank, the flow of water during treatment should be uniform to improve treatment efficiency, and the flow of the carrier during washing should not be obstructed and should be gentle. It is necessary to improve the cleaning efficiency, suppress the outflow of solids into the treated water, and evenly collect water at a low flow rate to suppress outflow of the solids and outflow of the carrier into the treated water.

【0004】[0004]

【発明が解決しようとする課題】移動床式好気性ろ床槽
は鋼板で製造していたが、何基もまとめて設置する場合
には、鋼板製よりもRC造りの方が設置コスト面で有利
であり、単一槽を複数台造るより、マルチタイプ(多槽
式)の方が一層有利である。また、鋼板製の好気性ろ床
槽においては、缶体の周囲および中央下部から集水する
機構を有していたが、RC造りの好気性ろ床槽では周囲
に集水機構を設置することは困難であり、中央下部の集
水機構のみでは、集水面積が不足して流速が早くなり、
担体の流出、処理水質の悪化が起こって前述のを満足
しない。担体の流出を抑えるため、集水導入箇所にスク
リーンを取り付けることで対応することも試みられてい
るが、原水の性状によっては目詰まりを起こし、運転停
止で担体を取り除く必要があるなどメンテナンスが煩雑
となる。そこで、本発明では、前述のを満足する
ろ床槽内部に、エアリフト管の周りに集水面積を大きく
とった集水機構を組み込むことにより、流速が均一で、
担体の流出がなく、処理水質の良好な移動床式好気性ろ
床槽の担体流出防止機構を提供することを目的とする。
The moving-bed aerobic filter bed tank was manufactured from steel plates, but when installing a number of units together, RC construction is more cost effective than steel plate construction. It is advantageous, and the multi-type (multi-tank type) is more advantageous than making a plurality of single tanks. Further, the steel plate aerobic filter bed has a mechanism for collecting water from the periphery of the can body and the lower center part. However, an aerobic filter bed made of RC should have a water collecting mechanism around it. Is difficult, and with only the water collecting mechanism in the lower center, the water collecting area is insufficient and the flow velocity becomes faster.
Outflow of the carrier and deterioration of treated water quality occur, and the above conditions are not satisfied. In order to suppress the outflow of the carrier, it has been attempted to install a screen at the water collection introduction point, but depending on the nature of the raw water, clogging may occur and it is necessary to remove the carrier by stopping the operation. Becomes Therefore, in the present invention, in the filter bed tank satisfying the above, by incorporating a water collecting mechanism having a large water collecting area around the air lift pipe, the flow velocity is uniform,
An object of the present invention is to provide a carrier outflow prevention mechanism for a moving bed type aerobic filter bed tank in which the carrier does not flow out and the treated water quality is good.

【0005】[0005]

【課題を解決するための手段】上記目的を達成するた
め、本発明は、担体を充填した好気性ろ床槽の上部から
原水を流入させ、ろ床槽内を下降する間に原水中の微細
な固形物を担体により捕捉し、水に溶け込んだ汚れは担
体表面に付着した微生物により分解したのち、生物処理
による固形物を付着させて下降した担体を、ろ床槽の中
央に設けたエアリフト管よって上昇させたのち、固形物
を分離した担体をろ床槽内へ循環させる一方、担体流出
防止機構によって担体の流出を防止しながらろ床槽の集
水域から処理水を槽外に流出させるようにした下降流式
水処理装置であって;前記担体流出防止機構は、ろ床槽
の集水域内に下降する担体を拡散させるためエアリフト
管の保護管の外周に設けた拡散傘と、拡散傘の小径側か
らろ床槽における反応域の半ばに達する高さに延びて担
体の流出を防止しうる集水筒と、集水筒の上部外壁から
槽外に突出させた処理水流出管と、からなることを特徴
とする。また、前記好気性ろ床槽は、鋼鉄製又は鉄筋コ
ンクリート造りの単一槽式もしくは多槽式であることを
特徴とする。
In order to achieve the above-mentioned object, the present invention allows raw water to flow from the upper part of an aerobic filter tank filled with a carrier, and fine particles in the raw water are supplied while descending in the filter bed tank. A solid substance is captured by a carrier, and dirt dissolved in water is decomposed by microorganisms adhering to the surface of the carrier. Therefore, after raising the carrier, the carrier from which the solid matter has been separated is circulated into the filter bed tank, while the carrier outflow prevention mechanism prevents the outflow of the carrier so that the treated water flows out from the catchment area of the filter bed tank. And a diffusing umbrella provided on the outer circumference of a protective pipe of an air lift pipe for diffusing the carrier descending into the catchment area of the filter bed tank, and a diffusing umbrella. From the small diameter side of the Extending to a height reaching the mid-range to the current water bottle capable of preventing the outflow of the carrier, the treated water outlet pipe from the upper outer wall is protruded outside the tank of the condenser water bottle, characterized in that it consists of. Further, the aerobic filter tank is characterized by being a single tank type or a multi-tank type made of steel or reinforced concrete.

【0006】[0006]

【発明の実施の形様】図1は本発明担体流出防止機構の
断面図である。図示のように、この下降流式水処理装置
は、RC造りの移動床式好気性ろ床槽10と、ろ床槽の上
部に設けた原水流入管13と、ろ槽内に空気を吹き込む
散気装置35と、ろ床槽内に充填した担体を上昇させる
エアリフト管29と、エアリフト管29の拡散傘付保護
管25と、保護管25の下部近くで床槽内の集水域12
に設けられて沈降する担体を拡散させる拡散傘26と、
エアリフト管29の上端に設けた担体分離装置20と、
拡散傘26の上部におけるエアリフト管29の周囲に設
けた集水機構30と、集水機構30から槽外に導出した
処理水流出管14とを主要部としている。
BEST MODE FOR CARRYING OUT THE INVENTION FIG. 1 is a sectional view of a carrier outflow prevention mechanism of the present invention. As shown in the figure, this down-flow type water treatment device comprises a moving-bed aerobic filter bed tank 10 made of RC, a raw water inflow pipe 13 provided at an upper part of the filter bed tank, and a blower for blowing air into the filter tank. Air device 35, an air lift pipe 29 for raising the carrier filled in the filter bed tank, a protective tube 25 with a diffusion umbrella of the air lift tube 29, and a water collecting area 12 in the floor tank near the lower part of the protection tube 25.
A diffusing umbrella 26 which is provided in the diffusing unit and which diffuses the sedimenting carrier;
A carrier separating device 20 provided at the upper end of the air lift pipe 29;
The water collecting mechanism 30 provided around the air lift pipe 29 in the upper part of the diffusion umbrella 26 and the treated water outflow pipe 14 led out of the tank from the water collecting mechanism 30 are the main parts.

【0007】好気性ろ床槽10は反応域である中央集水
部11と下部ホッパー形の集水域12とからなり、内部
に充填した担体(濾材)によって濾過層が形成されてい
る。担体としては、粒径は2〜10mm程度のアンスラ
サイト、活性炭、軽量骨材等が用いられる。集水域12
をホッパー形として生物処理によって生じた固形物を付
着させた担体を滞留させることなく、エアリフト管29
に吸い込ませる。
The aerobic filter tank 10 is composed of a central water collecting portion 11 which is a reaction area and a lower hopper type water collecting area 12, and a filter layer is formed by a carrier (filter material) filled inside. As the carrier, anthracite having a particle diameter of about 2 to 10 mm, activated carbon, lightweight aggregate or the like is used. Catchment area 12
The air-lift pipe 29 is made into a hopper shape without accumulating the carrier to which the solid matter generated by biological treatment adheres.
Suck it in.

【0008】好気性ろ床槽10の上部蓋16の中央に担
体分離装置20を設け、分離装置20の下部に吊り金具
を用いて集水域12の底近くにまで延びる拡散傘付保護
管25を吊り下げている。保護管25の上端部分はエア
流出防止用バッフル管28で包囲され、保護管25の内
部には、エア管18と担体上昇用のエアリフト管29を
挿通し、エア管18からの送気によって拡散傘26の下
方に滞留する担体をエアリフト管29によって上昇させ
る。すなわち、エアリフト管29の下端から原水の生物
処理によって固形物が付着した担体を吸い込むと共にエ
アリフト管29内で固形物を担体から剥離させながら固
形物と担体を同時に上昇させるものである。
A carrier separating device 20 is provided at the center of the upper lid 16 of the aerobic filter bed tank 10, and a protective pipe 25 with a diffusing umbrella extending to the vicinity of the bottom of the catchment area 12 is provided at the lower part of the separating device 20 by using a hanging metal fitting. It's hanging. The upper end portion of the protection tube 25 is surrounded by a baffle tube 28 for preventing air outflow, and the air tube 18 and an air lift tube 29 for raising the carrier are inserted into the protection tube 25 and diffused by the air supplied from the air tube 18. The carrier that accumulates below the umbrella 26 is lifted by the air lift pipe 29. That is, the solid substance is adsorbed from the lower end of the air lift pipe 29 by the biological treatment of the raw water, and the solid substance and the carrier are simultaneously raised while peeling the solid substance from the carrier in the air lift pipe 29.

【0009】エアリフト管29の上端には、担体と固形
物を分離して担体を好気性ろ床槽10内に循環させる分
離装置20がある。分離装置20は、図1に示すよう
に、エアリフト管29によって上昇した担体と固形物と
の混合物を分散下降させる担体分散傘23と、担体分散
傘23の下方に設けた担体取り出し用のスクリーン24
と、スクリーン24の下部に配置されて固形物を含む洗
浄排水を集める受け皿21と、洗浄排水受け皿21で受
けた排水を槽外に流出させる洗浄排水管15とからなっ
ている。スクリーン24は、担体を通さない程度の網目
を有するスリット、多孔板、金属メッシュ等が用いられ
る。また、排出する固形物の量は、エア管18の空気量
調節、スクリーン傾斜角の大小等によって制御すること
ができる。
At the upper end of the air lift pipe 29, there is a separating device 20 for separating the carrier and solid matter and circulating the carrier in the aerobic filter bed tank 10. As shown in FIG. 1, the separation device 20 includes a carrier dispersion umbrella 23 that disperses and descends a mixture of a carrier and a solid material that has been raised by an air lift pipe 29, and a carrier extraction screen 24 that is provided below the carrier dispersion umbrella 23.
And a tray 21 disposed below the screen 24 for collecting the washing wastewater containing solids, and a washing drainage pipe 15 for draining the drainage received by the washing drainage tray 21 to the outside of the tank. As the screen 24, a slit, a perforated plate, a metal mesh or the like having a mesh that does not allow the carrier to pass therethrough is used. In addition, the amount of solid matter to be discharged can be controlled by adjusting the amount of air in the air tube 18, adjusting the screen inclination angle, and the like.

【0010】拡散傘26は、図に示すように、円錐形を
なして集水筒31の下端に取り付けられている。処理水
流出管14は集水筒31の上部寄りからろ床槽10を貫
通して外部に導出されている。拡散傘26に集められた
処理水は、水位差によって処理水槽に上昇するようにな
っている。散気装置35は拡散傘の上部に設けられてい
る。このため、酸素が平均に担体に供給されその表面に
は微生物が付着成育している。エアリフト管29はその
下端を好気性ろ床槽10の底部に位置させると共に、そ
の上端をろ床槽10の上部に位置させている。
As shown in the figure, the diffusing umbrella 26 has a conical shape and is attached to the lower end of the water collecting cylinder 31. The treated water outflow pipe 14 penetrates the filter bed tank 10 from the upper part of the water collecting cylinder 31 and is led to the outside. The treated water collected by the diffusing umbrella 26 rises to the treated water tank due to the difference in water level. The air diffuser 35 is provided on the upper part of the diffusing umbrella. Therefore, oxygen is supplied to the carrier evenly, and microorganisms adhere to and grow on the surface of the carrier. The air lift pipe 29 has its lower end located at the bottom of the aerobic filter bed tank 10 and its upper end located at the upper part of the filter bed tank 10.

【0011】好気性ろ床槽10は、原水を生物学的に処
理するための担体(濾材)を充填し、散気装置35から
空気を供給する。散気装置35は、エアヘッダー管3
6、36の間に複数の散気管37、37を配置してプロ
セスエア供給管38からの空気を槽内に吹き出し、好気
性微生物の作用を盛んにする。
The aerobic filter tank 10 is filled with a carrier (filter material) for biologically treating raw water, and air is supplied from the air diffuser 35. The air diffuser 35 is the air header tube 3
A plurality of air diffusing pipes 37, 37 are arranged between the pipes 6, 36 to blow the air from the process air supply pipe 38 into the tank to enhance the action of aerobic microorganisms.

【0012】担体流出防止機構30は、図に示すよう
に、ろ床槽の集水域12内に下降する担体を拡散させる
ためエアリフト管の保護管25の外周に設けた拡散傘2
6と、拡散傘26の小径側からろ床槽における中央集水
部(反応域)11の半ばに達する高さに延びて担体の沈
降により流出を防止しながら処理水を低流速で均一に集
水する集水筒31と、集水筒31の上部外壁から槽外に
突出させた処理水流出管14と、から構成されている。
なお、図1中、符号32は集水筒31と拡散傘26との
接続位置に設けたサポート、17は槽上部架台、40は
エアヘッダードレン管である。
The carrier outflow prevention mechanism 30 is, as shown in the figure, a diffusing umbrella 2 provided on the outer periphery of a protective pipe 25 of an air lift pipe for diffusing the carrier descending into the catchment area 12 of the filter bed tank.
6 and from the small diameter side of the diffusion umbrella 26 to a height reaching the middle of the central water collecting part (reaction area) 11 in the filter bed tank, and preventing the outflow due to the sedimentation of the carrier, and uniformly collecting the treated water at a low flow rate. It is composed of a water collecting cylinder 31 for water and a treated water outflow pipe 14 protruding from the upper outer wall of the water collecting cylinder 31 to the outside of the tank.
In FIG. 1, reference numeral 32 is a support provided at a connection position between the water collecting cylinder 31 and the diffusing umbrella 26, 17 is a tank upper mount, and 40 is an air header drain pipe.

【0013】次に本発明の作用を説明する。担体(濾
材)を充填したろ床の下部の散気装置35から空気を吹
き込みながら、原水流入管13より流入させると、担体
の表面に無数の好気性微生物が繁殖する。槽内の上から
下に流れる間に原水中の微細な固形物は担体に捕捉され
る。水に溶け込んだ汚れは担体表面に付着した微生物に
より分解されて、下部の集水機構30からはきれいな水
(処理水)が出る。ろ床は徐々に閉塞してくるため、定
期的に下部から水と空気を吹き込んでエアリフトを運転
し、エアリフト管内で担体を洗浄し循環使用する。好気
性ろ床槽10内に充填された担体には、散気装置35に
よって曝気用空気が供給され、担体表面には微生物が付
着成育した状態になっている。原水流入管13によって
供給された原水は、ろ床槽内に形成された濾過層を通過
する。原水中に含まれるSS成分及びBOD成分等は微
生物の好気性生物処理によって酸化分解され、その結
果、担体表面には固形物が付着蓄積する。原水中の固形
物及び生物処理により発生した固形物は、担体表面ある
いは担体間に補集されており、捕集されたまま、濾過層
の下層へ移動していき、エアリフト管29より分離装置
20へ導かれる。そのため、処理水中の固形物混入が少
なく、通常の接蝕酸化法、活性汚泥法、散水ろ床法等に
おける沈澱池が不要となる。原水は濾過層を遭遇する際
に浄化されつつ、重力作用及びエアリフト装置によって
生じたエアリフト管29の下端への吸込力によって好気
性ろ床槽10の上部から下向きに流れる。
Next, the operation of the present invention will be described. When air is blown from the raw water inflow pipe 13 while blowing air from the air diffuser 35 below the filter bed filled with the carrier (filter medium), numerous aerobic microorganisms propagate on the surface of the carrier. Fine solids in the raw water are captured by the carrier while flowing from the top to the bottom in the tank. The dirt dissolved in the water is decomposed by the microorganisms adhering to the surface of the carrier, and clean water (treated water) is discharged from the water collecting mechanism 30 below. Since the filter bed is gradually closed, water and air are periodically blown from the lower part to operate the air lift, and the carrier is washed and circulated in the air lift pipe. Air for aeration is supplied to the carrier filled in the aerobic filter bed tank 10 by the air diffuser 35, and microorganisms are attached and grown on the surface of the carrier. The raw water supplied by the raw water inflow pipe 13 passes through the filtration layer formed in the filter bed tank. The SS component and BOD component contained in the raw water are oxidatively decomposed by the aerobic treatment of microorganisms, and as a result, solid matter is attached and accumulated on the surface of the carrier. The solid matter in the raw water and the solid matter generated by biological treatment are collected on the surface of the carrier or between the carriers, and while being collected, move to the lower layer of the filtration layer, and are separated from the air lift pipe 29 to the separation device 20. Be led to. Therefore, the solid content in the treated water is small, and the sedimentation basin in the usual corrosive oxidation method, activated sludge method, sprinkling filter method, etc. becomes unnecessary. The raw water is purified when it encounters the filter layer, and flows downward from the upper part of the aerobic filter bed tank 10 by the gravity force and the suction force to the lower end of the air lift pipe 29 generated by the air lift device.

【0014】濾過層によって浄化された処理水は好気性
ろ床槽の底部に向かつて流れるが、ろ床槽10の下部に
は拡散傘26を有するホッパー形集水域12が形成され
ているので、処理水の一部はエアリフト管29の下端に
吸い込まれるが、多くは集水機構30に吸い込まれ処理
水流出管14を介して処理水槽(図示せず)内に導かれ
る。集水機構30は、拡散傘26と、比較的長い集水筒
31を持ち、また、集水筒31の上部寄りに処理水流出
管流入口14をセットしてあるので、処理時の水の流れ
を均一にして、処理効率を上げ、処理水への固形物や担
体の流出を抑えて良好な処理水を得ることができる。
The treated water purified by the filtration layer flows toward the bottom of the aerobic filter tank, but since the hopper-shaped catchment area 12 having the diffusion umbrella 26 is formed in the lower part of the filter bed tank 10, A part of the treated water is sucked into the lower end of the air lift pipe 29, but most of the treated water is sucked into the water collecting mechanism 30 and introduced into the treated water tank (not shown) through the treated water outflow pipe 14. The water collecting mechanism 30 has the diffusion umbrella 26 and a relatively long water collecting cylinder 31, and the treated water outlet pipe inlet 14 is set near the upper part of the water collecting cylinder 31, so that the flow of water during treatment is It is possible to obtain uniform treated water by increasing the treatment efficiency, suppressing the outflow of solid matters and carriers into the treated water, and obtaining good treated water.

【0015】一方、固形物の付着した担体は、エア管1
8から吹き込まれたエアリフト用空気により、エアリフ
ト管29の下端より吸い込まれて管内を上昇する。エア
リフト管29内を担体、処理水の一部、空気が上昇する
ため、固形物は、攪拌され、担体から分離される。汚れ
た担体を空気によりもみ洗い、逆流することなく連続運
転される。この分離した固形物、担体、処理水の一部は
エアリフト管29を上昇して、その上端から分離装置2
0に排出される。この時、固形物、担体、処理水の一部
(通常この処理水は逆洗水と呼ばれる)は分離装置20
の遮蔽板によって遮られ傾斜面に沿って流れる。エアリ
フト管29内で洗浄された担体は、分離装置の傾斜する
スクリーン24にかけられ、ろ床槽10内に循環する。
固形物は分離装置20の中空構造部内に逆洗水と共に入
り込む。この固形物は、逆洗水と共に逆洗排水となる。
この逆洗排水は、洗浄排水受け皿21で受け、排水管1
5によって排出される。
On the other hand, the carrier to which the solid matter is attached is the air tube 1
Air for air lift blown from 8 is sucked from the lower end of the air lift pipe 29 and rises in the pipe. Since the carrier, part of the treated water, and air rise in the air lift pipe 29, the solid matter is agitated and separated from the carrier. The dirty carrier is scrubbed with air and continuously operated without backflow. The separated solid matter, carrier, and part of the treated water rise in the air lift pipe 29, and are separated from the upper end of the separation device 2
It is discharged to 0. At this time, the solid matter, the carrier, and part of the treated water (usually this treated water is called backwash water) are separated by the separator 20.
It is blocked by the shield plate and flows along the inclined surface. The carrier washed in the air lift pipe 29 is hung on the inclined screen 24 of the separator and circulated in the filter bed tank 10.
The solid matter enters the hollow structure of the separating device 20 together with the backwash water. This solid matter becomes backwash drainage together with backwash water.
The backwash drainage is received by the wash drainage tray 21 and the drain pipe 1
Discharged by 5.

【0016】[0016]

【発明の効果】上記のように、本発明は、スクリーンが
ないため、目詰まりの恐れがなく、原水性状に対する適
応が広がった。槽本体の溶接個所が少なく、構造が簡素
化され加工性が向上する。また、担体流出防止機構は、
ろ床槽の集水域内に下降する担体を拡散させるためエア
リフト管の保護管の外周に設けた拡散傘と、拡散傘の小
径側からろ床槽における反応域の半ばに達する高さに延
びて担体の沈降により流出を防止しながら処理水を低流
速で均一に集水する集水筒と、集水筒の上部外壁から槽
外に突出させた処理水流出管と、から構成されているた
め、低流速で担体の移動を妨げることなく均一集水して
処理効率を上げると共に、処理水への担体および固形物
の流出を抑えることにより良好な処理水を得ることがで
きる。また、鋼板製又は鉄筋コンクリート造りの単一槽
式もしくはマルチタイプの好気性ろ床槽とすることによ
り、設置コストの低減をはかることが可能である。
As described above, according to the present invention, since there is no screen, there is no fear of clogging, and the application to the raw water state is widened. There are few welding points on the tank body, the structure is simplified and the workability is improved. In addition, the carrier outflow prevention mechanism
A diffusing umbrella provided on the outer periphery of the protective tube of the air lift pipe for diffusing the carrier descending into the catchment area of the filter bed tank, and extending from the small diameter side of the diffusing umbrella to a height reaching the middle of the reaction area in the filter bed tank. Since it is composed of a water collection tube that uniformly collects the treated water at a low flow rate while preventing the outflow due to the sedimentation of the carrier, and a treated water outflow pipe protruding from the upper outer wall of the water collection tube to the outside of the tank, It is possible to obtain good treated water by uniformly collecting water without disturbing the movement of the carrier at the flow rate to improve the treatment efficiency and suppressing the outflow of the carrier and solids into the treated water. Further, by using a single tank type or multi-type aerobic filter bed tank made of steel plate or reinforced concrete, it is possible to reduce the installation cost.

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

【図1】 本発明方法を実施する装置の断面図である。1 is a cross-sectional view of an apparatus for carrying out the method of the present invention.

【符号の説明】[Explanation of symbols]

10 好気性ろ床槽 11 中央集水
部 12 下部ホッパー形集水域 13 原水流入
管 14 処理水流出管 15 洗浄排水
管 16 上部蓋 17 槽上部架
台 18 エア管 20 分離装置 21 洗浄排水受皿 22 集合受皿
用ブラケット 23 担体分散傘 24 スクリー
ン 25 拡散傘付保護管 26 拡散傘 29 エアリフト管 28 エア流出
防止用バッフル管 30 集水機構 31 集水筒 32 サポート 35 散気装置 36 エアヘッダー管 37 散気管 38 プロセスエア供給管 40 エアヘッ
ダードレン管
10 Aerobic filter tank 11 Central water collecting part 12 Lower hopper type water collecting area 13 Raw water inflow pipe 14 Treated water outflow pipe 15 Washing drainage pipe 16 Upper lid 17 Tank upper mount 18 Air pipe 20 Separation device 21 Washing drainage tray 22 Collecting tray Bracket 23 carrier dispersion umbrella 24 screen 25 protective tube with diffuser umbrella 26 diffuser umbrella 29 air lift tube 28 air outflow prevention baffle tube 30 water collecting mechanism 31 water collecting tube 32 support 35 air diffuser 36 air header tube 37 air diffuser 38 process air Supply pipe 40 Air header drain pipe

───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 4D003 AA08 AB02 DA07 DA11 DA15 DA22 DA30 EA01 EA22 EA23 EA25    ─────────────────────────────────────────────────── ─── Continued front page    F-term (reference) 4D003 AA08 AB02 DA07 DA11 DA15                       DA22 DA30 EA01 EA22 EA23                       EA25

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 担体を充填した好気性ろ床槽の上部から
原水を流入させ、ろ床槽内を下降する間に原水中の微細
な固形物を担体により捕捉し、生物処理による固形物を
付着させて下降した担体を、ろ床槽の中央に設けたエア
リフト管よって上昇させたのち、固形物を分離した担体
をろ床槽内へ循環させる一方、担体流出防止機構によっ
て担体の流出を防止しながらろ床槽の集水域から処理水
を槽外に流出させるようにした下降流式水処理装置であ
って、 前記担体流出防止機構は、ろ床槽の集水域内に下降する
担体を拡散させるためエアリフト管の保護管の外周に設
けた拡散傘と、拡散傘の小径側からろ床槽における反応
域の半ばに達する高さに延びて担体の流出を防止しうる
集水筒と、集水筒の上部外壁から槽外に突出させた処理
水流出管と、からなることを特徴とする水処理装置の担
体流出防止機構。
1. Raw water is introduced from the upper part of an aerobic filter bed filled with a carrier, and fine solids in the raw water are captured by the carrier while descending in the filter bed tank to remove solid matter by biological treatment. The carrier that has adhered and descended is raised by an air lift pipe provided in the center of the filter bed tank, and then the carrier from which solids have been separated is circulated into the filter bed tank, while the carrier outflow prevention mechanism prevents the carrier from flowing out. While being a downward flow type water treatment device configured to allow treated water to flow out of the catchment area of the filter bed tank, the carrier outflow prevention mechanism diffuses carriers descending into the catchment area of the filter bed tank. A diffusing umbrella provided on the outer periphery of the protective tube of the air lift pipe, a water collecting cylinder that can prevent the outflow of the carrier by extending from the small diameter side of the diffusing umbrella to a height reaching the middle of the reaction area in the filter bed tank, and a water collecting cylinder With the treated water outflow pipe protruding from the upper outer wall of the Carrier outflow preventing mechanism of the water treatment apparatus characterized by comprising a.
【請求項2】 前記好気性ろ床槽は、鋼板製又は鉄筋コ
ンクリート造りの単一槽式もしくは多槽式であることを
特徴とする請求項1に記載の下降流式水処理装置の担体
流出防止機構。
2. The carrier outflow prevention of a downflow type water treatment device according to claim 1, wherein the aerobic filter bed tank is a single tank type or a multi-tank type made of steel plate or reinforced concrete. mechanism.
JP2001390401A 2001-10-25 2001-12-21 Carrier outflow prevention mechanism for water treatment equipment Expired - Lifetime JP3831661B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001390401A JP3831661B2 (en) 2001-10-25 2001-12-21 Carrier outflow prevention mechanism for water treatment equipment

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP2001327828 2001-10-25
JP2001-327828 2001-10-25
JP2001390401A JP3831661B2 (en) 2001-10-25 2001-12-21 Carrier outflow prevention mechanism for water treatment equipment

Publications (2)

Publication Number Publication Date
JP2003200185A true JP2003200185A (en) 2003-07-15
JP3831661B2 JP3831661B2 (en) 2006-10-11

Family

ID=27666498

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

Country Link
JP (1) JP3831661B2 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103781525A (en) * 2011-09-07 2014-05-07 熊津豪威株式会社 Continuous circulation sand filter and continuous circulation sand filtering method
CN105967262A (en) * 2016-06-27 2016-09-28 杭州回水科技股份有限公司 Dephosphorizing granular activated coke adsorption tower with fluidized bed
CN106006818A (en) * 2016-06-27 2016-10-12 杭州回水科技股份有限公司 Multi-stage adsorption tower adopting phosphorus-removing granular active coke
CN116514269A (en) * 2023-04-15 2023-08-01 广州清源凯旋环保科技有限公司 Fluidized bed reactor by biomembrane method and process for treating formaldehyde wastewater with wide-area concentration

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103781525A (en) * 2011-09-07 2014-05-07 熊津豪威株式会社 Continuous circulation sand filter and continuous circulation sand filtering method
US9567241B2 (en) 2011-09-07 2017-02-14 Coway Entech Co., Ltd Continuous circulation sand filter and continuous circulation sand filtering method
CN105967262A (en) * 2016-06-27 2016-09-28 杭州回水科技股份有限公司 Dephosphorizing granular activated coke adsorption tower with fluidized bed
CN106006818A (en) * 2016-06-27 2016-10-12 杭州回水科技股份有限公司 Multi-stage adsorption tower adopting phosphorus-removing granular active coke
CN116514269A (en) * 2023-04-15 2023-08-01 广州清源凯旋环保科技有限公司 Fluidized bed reactor by biomembrane method and process for treating formaldehyde wastewater with wide-area concentration
CN116514269B (en) * 2023-04-15 2023-10-31 广州清源凯旋环保科技有限公司 Fluidized bed reactor by biomembrane method and process for treating formaldehyde wastewater with wide-area concentration

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