JPH05177193A - Aeration method and device therefor - Google Patents

Aeration method and device therefor

Info

Publication number
JPH05177193A
JPH05177193A JP3359851A JP35985191A JPH05177193A JP H05177193 A JPH05177193 A JP H05177193A JP 3359851 A JP3359851 A JP 3359851A JP 35985191 A JP35985191 A JP 35985191A JP H05177193 A JPH05177193 A JP H05177193A
Authority
JP
Japan
Prior art keywords
tank
aeration
flow
water
cylindrical body
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.)
Pending
Application number
JP3359851A
Other languages
Japanese (ja)
Inventor
Teruhisa Yoshida
輝久 吉田
Koichi Mizuta
耕市 水田
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.)
Hitachi Kiden Kogyo Ltd
Original Assignee
Hitachi Kiden Kogyo 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 Hitachi Kiden Kogyo Ltd filed Critical Hitachi Kiden Kogyo Ltd
Priority to JP3359851A priority Critical patent/JPH05177193A/en
Publication of JPH05177193A publication Critical patent/JPH05177193A/en
Pending 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

  • Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
  • Mixers Of The Rotary Stirring Type (AREA)

Abstract

PURPOSE:To agitate uniformly even in the bottom section of a deep tank, supply air or oxygen of desired amount and carry out aeration efficiently. CONSTITUTION:A self-suction aeration machine 4 for generating water flow by the rotation of a screw 41 and sucking air by the negative pressure generated at the end of the screw 41, a cylindrical body 2 provided below the aeration machine 4 and an agitator 3 forming downward flow in the cylindrical body 2 are installed in an aeration tank 1. Circulating flow generated in the aeration tank 1 by driving aeration machine 4 and the agitator 3, and the foams blown into water in the shallow position of the water are transferred to the bottom section of the tank 1 by the downward flow in the cylindrical body 2 and jetted as upward flow in the outer peripheral section of the cylindrical body 2 to carry out the agitation and aeration covering whole the inside of tank 1 uniformly.

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10数m以上の深槽の槽
底部においても均一に撹拌し、かつ所要量の空気または
酸素を供給し、効率的に曝気を行う方法及びその装置に
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 aerating efficiently by uniformly agitating even at the bottom of a deep tank having a depth of 10 m or more and supplying a required amount of air or oxygen. Is.

【0002】[0002]

【従来の技術】汚水処理において、汚水中の有機物を分
解処理する方法として槽内に空気を供給し、汚水を撹拌
する曝気方法がある。従来深槽の汚水にしかも槽部まで
撹拌し、曝気するものとして特公昭55−29756号
公報に開示されたものがある。これは槽内に円筒を配設
し、この円筒内にスクリューを設け、これにより円筒内
の汚水に空気を吹き込みつつ下向流を発生させ、槽底に
達した後、円筒の外周部を上向流として槽内を循環させ
る方法である。
2. Description of the Related Art In the treatment of sewage, there is an aeration method in which air is supplied into a tank and sewage is agitated as a method of decomposing and treating organic matter in sewage. Conventionally, there is one disclosed in Japanese Examined Patent Publication No. 55-29756 for aeration by agitating the sewage in a deep tank and further agitating the tank. This consists of arranging a cylinder in the tank, and installing a screw in this cylinder to generate a downward flow while blowing air into the sewage in the cylinder, and after reaching the bottom of the tank, the outer periphery of the cylinder is raised. This is a method of circulating in the tank as a countercurrent.

【0003】[0003]

【発明が解決しようとする課題】槽内に設置した円筒内
に撹拌機にて下向流を発生させて、円筒内の汚水を撹拌
しつつ、空気を吹き込み槽底まで流下させる場合、10
数m程度の槽では槽内全体循環流が発生し、所要の撹拌
と曝気とが行える。しかし汚水の下向流中に曝気する場
合、円筒内にはこの撹拌機による下向流の一部に、円筒
内を上昇する気泡によりある程度の上向流が発生する。
これは気泡によるエアリフト力により一般にその発生上
向流は約0.3m/Sとなっている。従って10m以上
の深槽においてはこのエアリフト力による上向流により
下向水流及び空気が槽底部にまで達せず槽内の均一撹拌
及び曝気ができなかった。
When a downward flow is generated by a stirrer in a cylinder installed in the tank to stir sewage in the cylinder and air is blown down to the bottom of the tank, 10
In a tank of about several meters, the entire circulation flow in the tank is generated, and required agitation and aeration can be performed. However, when aeration is performed in the downward flow of sewage, a certain amount of upward flow is generated in the cylinder due to the bubbles rising in the cylinder in a part of the downward flow of the stirrer.
Due to the air lift force of the bubbles, the generated upward flow is generally about 0.3 m / S. Therefore, in a deep tank of 10 m or more, the downward flow of water and air did not reach the bottom of the tank due to the upward flow due to the air lift force, and uniform stirring and aeration in the tank were not possible.

【0004】本発明では曝気機にさらに撹拌用のスクリ
ューを備え、強水流を発生させて10m以上の深い槽に
おいても槽内全体にわたる循環流を発生させ、酸素供給
と混合撹拌を安定して行い所望の撹拌・曝気を槽底部ま
で均一に行うことを目的とする。
In the present invention, the aerator is further equipped with a screw for stirring to generate a strong water flow to generate a circulating flow throughout the tank even in a deep tank of 10 m or more to stably supply oxygen and perform mixing and stirring. The purpose is to perform desired stirring and aeration evenly to the bottom of the tank.

【0005】[0005]

【課題を解決するための手段】本発明は上記目的を達成
するためになしたもので、スクリューの旋回により水流
を発生させ、スクリュー先端に発生する負圧にて吸気す
る自吸式曝気機と、この曝気機の下方位に設けた円筒体
と、この円筒体内にて下向流を形成する撹拌機とを曝気
槽内に設け、この曝気機・撹拌機を駆動して曝気槽内に
循環流を発生させるとともに水深の浅い位置で水中に吹
き込まれた気泡を円筒体内の下向流にて槽底部へ移行さ
せ、円筒体外周部にて上向流として噴出せしめて槽内全
体の撹拌と曝気を均一にて行うことを要旨とする。
The present invention has been made to achieve the above object, and a self-priming aerator for generating a water flow by swirling a screw and sucking at a negative pressure generated at the tip of the screw. , A cylinder provided in the lower direction of the aerator and a stirrer that forms a downward flow in the cylinder are provided in the aeration tank, and the aerator / agitator is driven to circulate in the aeration tank. The flow of air is generated and the bubbles blown into the water at a shallow depth are transferred to the bottom of the tank by the downward flow of the cylinder, and are jetted as an upward flow at the outer circumference of the cylinder to agitate the entire tank. The point is to perform aeration uniformly.

【0006】[0006]

【作用】自吸式曝気機を水面近傍に設置して、水中に空
気を吹き込んで曝気をする場合、曝気により生成された
気泡がエアリフト力となり、底に向かう流水速度が打ち
消され、短時間のうちに上向流となって上昇し始める。
このため10m以上の深い槽においては水流及び気泡が
槽底部に到達せず、槽内の曝気・撹拌が行えない。しか
し本発明のように水面近傍に曝気機を設置し、この下方
に撹拌翼を設置することにより円筒(ドラフトチュー
ブ)内で下向流が1m/秒以上となるよう曝気機・撹拌
機を運転することにより深い槽においてもこの気泡によ
るエアリフト力に打ち消されることがなく、水面から吹
き込んだ気泡状空気または酸素を槽底部まで移行させら
れ、この気泡を槽底部より再び上昇させて槽内汚水の撹
拌混合を行い、均一な曝気が行える。
[Operation] When a self-priming aerator is installed near the water surface and air is blown into the water for aeration, the air bubbles generated by the aeration act as an air lift force, which cancels the flowing water velocity toward the bottom, and It becomes an upward flow and begins to rise.
For this reason, in a deep tank of 10 m or more, water flow and air bubbles do not reach the bottom of the tank, and aeration and stirring inside the tank cannot be performed. However, by installing an aerator near the water surface and installing a stirring blade below this as in the present invention, the aerator / agitator is operated so that the downward flow is 1 m / sec or more in the cylinder (draft tube). By doing so, even in a deep tank, it is not canceled by the air lift force due to this bubble, bubble-like air or oxygen blown from the water surface can be transferred to the bottom of the tank, and this bubble is raised again from the bottom of the tank to recycle wastewater in the tank. Uniform aeration can be performed by stirring and mixing.

【0007】[0007]

【実施例】以下本発明曝気方法及びその装置を図示の実
施例にもとづいて説明する。図において1は所要の容積
及び10m以上の深さを有する矩形等の曝気槽で、この
曝気槽1内中央部に、撹拌機及び自吸式曝気機の撹拌に
て槽内全体の汚水に、槽上部と槽底部とにて循環水流を
生じるよう円筒体2(ドラフトチューブ)を上下方向に
配設し、かつこの円筒体2の上端と下端には水面及び槽
底から汚水を循環させるために適当な間隔を開けるよう
になす。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The aeration method and apparatus of the present invention will be described below with reference to the illustrated embodiments. In the figure, 1 is a rectangular aeration tank having a required volume and a depth of 10 m or more. At the center of the aeration tank 1, the agitator and a self-priming aerator agitate the whole sewage in the tank. A cylindrical body 2 (draft tube) is arranged vertically so as to generate a circulating water flow between the upper part and the lower part of the tank, and the upper and lower ends of the cylindrical body 2 are for circulating sewage from the water surface and the bottom of the tank. Make an appropriate space.

【0008】円筒体2内には上方位置に曝気機4をその
下方位置に撹拌機3を設置するが、この円筒体2は円柱
に限定されることなく角筒形であってもよく、さらに曝
気機4はそのスクリュー41が水面近傍になるように設
置し、モータ42にて駆動される中空軸43の下端にス
クリュー41が固定され、このスクリュー41の回動に
て円筒体内で、かつスクリュー先端水域に生じる負圧に
て中空軸上端より吸気し、水中へ微細気泡として水中へ
放出するようになす。
The aerator 4 is installed in the upper position of the cylindrical body 2 and the agitator 3 is installed in the lower position thereof, but the cylindrical body 2 is not limited to the cylindrical shape, and may be a rectangular cylindrical shape. The aerator 4 is installed so that its screw 41 is near the water surface, and the screw 41 is fixed to the lower end of a hollow shaft 43 driven by a motor 42. The rotation of this screw 41 causes the screw 41 to move in the cylinder and The negative pressure generated in the tip water area sucks air from the upper end of the hollow shaft and discharges it into the water as fine bubbles.

【0009】撹拌機3はこの曝気機4のスクリュー41
より下方位置に設置され、水中モータ31にて撹拌スク
リュー32を回動するようになすとともに、この撹拌ス
クリューにて発生する下向水流速が円筒体下端の槽底部
まで充分に達するものとし、気泡によるエアリフト力の
上向流0.3m/秒を打ち消す以上の1.0m/秒とす
る。
The agitator 3 is a screw 41 of the aerator 4.
It is installed at a lower position and the stirring screw 32 is rotated by the submersible motor 31, and the downward flow velocity of water generated by the stirring screw reaches the bottom of the cylinder at the bottom of the cylinder sufficiently. The upward flow of 0.3 m / sec caused by the air lift force is set to 1.0 m / sec, which is more than the cancellation.

【0010】撹拌機3は図1に示すように水中にその全
体を設置するか、図2に示すようにモータ等の駆動部3
1を水面上方で、円筒体2の中央部に設置し、比較的長
い軸32の下端にスクリュー33を固定し、これにより
1.0m/秒以上の下向流を発生させるようにし、下向
流を槽底部まで達成するようになす。そして曝気機4は
この撹拌機3を挟んで、円筒体内にその中央より少し位
置が外れたところに1台もしくは2台以上設置する。こ
の曝気機4はその構造、水面よりの設置位置は図1の実
施例と同様とする。
The stirrer 3 is installed in water as a whole as shown in FIG. 1, or as shown in FIG.
1 is installed in the center of the cylindrical body 2 above the water surface, and a screw 33 is fixed to the lower end of a relatively long shaft 32 so that a downward flow of 1.0 m / sec or more is generated. The flow is made to reach the bottom of the tank. Then, one or two or more aerators 4 are installed in the cylindrical body with the agitator 3 sandwiched therebetween, at a position slightly displaced from the center thereof. The structure and the installation position of the aerator 4 from the water surface are the same as those in the embodiment of FIG.

【0011】さらに図3は撹拌機3と曝気機4を一体と
した実施例を示し、水面上方に設置されたモータ50に
て円筒体2の中央に配設するようにした中空軸51を駆
動し、この中空軸51の下端に撹拌用のスクリュー3a
を、これよりも上方位置に曝気用のスクリュー4aを夫
々設け、かつ中空軸上端に吸気量制御用のバルブ6を設
け、これにより同一のモータにて撹拌と曝気とを行うも
のである。
Further, FIG. 3 shows an embodiment in which the agitator 3 and the aerator 4 are integrated, and a hollow shaft 51 which is arranged at the center of the cylindrical body 2 is driven by a motor 50 installed above the water surface. At the lower end of this hollow shaft 51, a screw 3a for stirring is attached.
The aeration screws 4a are provided at positions higher than the above, and the intake air amount control valve 6 is provided at the upper end of the hollow shaft, whereby agitation and aeration are performed by the same motor.

【0012】図1に示す実施例において原水Aと返送汚
泥Bはともに円筒体2の上部から流入させ、曝気槽混合
液Cを槽1の上部側面より越流させ、別に設けた沈澱池
に送り、ここで汚泥と上澄水とに固液分離が行われる。
この混合液を取り出す位置Cは流入原水が短絡しない位
置であれば図示のように限定されることなく、どこでも
よい。
In the embodiment shown in FIG. 1, both the raw water A and the returned sludge B are made to flow in from the upper part of the cylindrical body 2, the aeration tank mixed liquid C is made to overflow from the upper side surface of the tank 1, and sent to a separate settling basin. Here, solid-liquid separation is performed into sludge and supernatant water.
The position C from which this mixed liquid is taken out is not limited as shown in the figure as long as it is a position where the inflowing raw water is not short-circuited, and it may be anywhere.

【0013】なお原水と返送汚泥は曝気によって気泡が
混在する混合液(循環水)よりも比重が重いため、曝気
位置の上部に流入させることにより気泡が円筒体内を下
向するのを推進させる効果が得られる。
Since the specific gravity of the raw water and the returned sludge is heavier than the mixed liquid (circulating water) in which air bubbles are mixed by aeration, the effect of promoting air bubbles downward in the cylindrical body by flowing into the upper part of the aeration position is obtained. Is obtained.

【0014】次に上述の装置における曝気運転について
説明する。曝気槽の運転開始時には、まず撹拌機3のみ
を運転し、円筒体2内に汚水を撹拌して下向流を発生さ
せ、槽底に達した後、円筒体外周部を上向するようにし
て槽内にその上部と底部間に円筒体内を介して循環水流
を発生させる。この循環水流の流速が気泡によるエアリ
フト力にて打ち消されない以上の下向流速例えば1m/
秒以上となったとき、曝気機4を運転する。
Next, the aeration operation in the above device will be described. At the start of operation of the aeration tank, first, only the stirrer 3 is operated to stir the dirty water in the cylindrical body 2 to generate a downward flow, and after reaching the tank bottom, the outer peripheral portion of the cylindrical body is directed upward. A circulating water flow is generated in the tank between the upper part and the bottom part through the cylindrical body. The downward flow velocity, for example, 1 m /, above which the flow velocity of this circulating water flow is not canceled by the air lift force of the bubbles.
When the number of seconds is exceeded, the aerator 4 is operated.

【0015】また曝気量が多いほど、また気泡の径が大
きいほど円筒体内を上昇しようとする浮力が大きくなる
ため、曝気機はできるだけ微細気泡を形成できるものを
用い、曝気開始時には曝気量を制限しながら徐々に増加
させることが望ましい。曝気量の制御は、図1のように
曝気機が1台のときは回転数を制御し、図2のように曝
気機を複数台設けるときは台数を制御、また図3のよう
に制御バルブ付のときはバルブ開度制御により行うこと
ができる。
Further, the larger the amount of aeration and the larger the diameter of the bubbles, the greater the buoyancy that tends to rise inside the cylinder. Therefore, an aerator that can form the finest bubbles as possible is used, and the aeration amount is limited at the start of aeration. However, it is desirable to gradually increase. The aeration amount is controlled by controlling the rotation speed when there is one aerator as shown in FIG. 1, and by controlling the number when a plurality of aerators is provided as shown in FIG. When attached, it can be performed by controlling the valve opening.

【0016】なお本発明において、円筒体口径が小さい
ほど小さい動力の撹拌機で1m/秒以上の下向流速が得
られるが、曝気槽平断面積に対する円筒体内の平面積が
小さくなり、円筒体外側の混合液を上昇させる効果が小
さくなる。従って本発明の曝気装置を設置する場合は曝
気槽平断面に対する円筒体口径を考慮して、本発明の曝
気装置を複数台設置するか、口径の大きい円筒体を1台
設置するかを検討する必要がある。
In the present invention, the smaller the diameter of the cylindrical body, the lower the flow velocity of 1 m / sec or more can be obtained with an agitator having a smaller power, but the plane area in the cylinder with respect to the plane cross-sectional area of the aeration tank becomes smaller, The effect of raising the liquid mixture on the outside is reduced. Therefore, when installing the aeration apparatus of the present invention, it is considered whether to install a plurality of the aeration apparatus of the present invention or to install one large-diameter cylindrical body in consideration of the diameter of the cylindrical body with respect to the plane cross section of the aeration tank. There is a need.

【0017】[0017]

【発明の効果】本発明によれば円筒体と撹拌機と自吸式
曝気機を設け、浅い水深に吹き込んだ気泡を撹拌機によ
り生じた円筒体内の下向流にのせて、深槽曝気槽底部ま
で移行させることにより、気泡が深槽で高い水圧を受け
て気泡中の酸素分圧が高まるともに、気泡の接触時間も
長くできるため、酸素の利用効率が極めて高く、省スペ
ースの深槽曝気槽で経済的に曝気することができ、また
水面上に駆動装置を設けているため、維持管理も容易と
いう効果を有する。
According to the present invention, a cylindrical body, a stirrer and a self-priming aerator are provided, and bubbles blown into a shallow water depth are placed on the downward flow of the cylindrical body generated by the stirrer to provide a deep tank aeration tank. By moving to the bottom, the bubbles receive high water pressure in the deep tank to increase the oxygen partial pressure in the bubbles, and the contact time of the bubbles can be lengthened, so the oxygen utilization efficiency is extremely high and space-saving deep tank aeration is possible. Aeration can be economically performed in the tank, and since the drive device is installed on the surface of the water, maintenance is easy.

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

【図1】本発明の第1実施例を示す説明図である。FIG. 1 is an explanatory diagram showing a first embodiment of the present invention.

【図2】同第2実施例を示す説明図である。FIG. 2 is an explanatory diagram showing the second embodiment.

【図3】同第3実施例を示す説明図である。FIG. 3 is an explanatory diagram showing the third embodiment.

【図4】公知例の説明図である。FIG. 4 is an explanatory diagram of a known example.

【符号の説明】[Explanation of symbols]

1 曝気槽 2 円筒体 3 撹拌機 4 曝気機 5 バルブ 1 Aeration tank 2 Cylindrical body 3 Stirrer 4 Aeration machine 5 Valve

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 スクリューの旋回により水流を発生さ
せ、スクリュー先端に発生する負圧にて吸気する自吸式
曝気機と、この曝気機の下方位に設けた円筒体と、この
円筒体内にて下向流を形成する撹拌機とを曝気槽内に設
け、この曝気機・撹拌機を駆動して曝気槽内に循環流を
発生させるとともに水深の浅い位置で水中に吹き込まれ
た気泡を円筒体内の下向流にて槽底部へ移行させ、円筒
体外周部にて上向流として噴出せしめて槽内全体の撹拌
と曝気を均一にて行うことを特徴とする曝気方法。
1. A self-priming aerator that generates a water flow by swirling a screw and inhales with a negative pressure generated at the tip of the screw, a cylinder provided in the lower direction of the aerator, and a cylinder inside the cylinder. A stirrer that forms a downward flow is installed in the aeration tank, and this aerator / stirrer is driven to generate a circulating flow in the aeration tank and bubbles blown into the water at a shallow water depth are placed inside the cylinder. The aeration method is characterized in that it is transferred to the bottom of the tank by the downward flow of the air, and is jetted as an upward flow at the outer peripheral portion of the cylindrical body to uniformly stir and aerate the entire inside of the tank.
【請求項2】 スクリューの旋回により水流を発生さ
せ、スクリュー先端に発生する負圧にて吸気する自吸式
曝気機と、この曝気機の下方位に設けた円筒体と、この
円筒体内にて下向流を形成する撹拌機とを曝気槽内に設
けたことを特徴とする曝気装置。
2. A self-priming aerator that generates a water flow by swirling a screw and inhales by a negative pressure generated at the tip of the screw, a cylinder body provided in the lower direction of the aerator, and a cylinder body inside the cylinder body. An aeration device, characterized in that a stirrer that forms a downward flow is provided in the aeration tank.
JP3359851A 1991-12-26 1991-12-26 Aeration method and device therefor Pending JPH05177193A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3359851A JPH05177193A (en) 1991-12-26 1991-12-26 Aeration method and device therefor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3359851A JPH05177193A (en) 1991-12-26 1991-12-26 Aeration method and device therefor

Publications (1)

Publication Number Publication Date
JPH05177193A true JPH05177193A (en) 1993-07-20

Family

ID=18466627

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3359851A Pending JPH05177193A (en) 1991-12-26 1991-12-26 Aeration method and device therefor

Country Status (1)

Country Link
JP (1) JPH05177193A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006289188A (en) * 2005-04-06 2006-10-26 Nishihara Environment Technology Inc Sewage treatment apparatus
JP2010535627A (en) * 2007-08-15 2010-11-25 ユナイテッド・ユーティリティーズ・ピーエルシー Method and apparatus for aeration

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006289188A (en) * 2005-04-06 2006-10-26 Nishihara Environment Technology Inc Sewage treatment apparatus
JP2010535627A (en) * 2007-08-15 2010-11-25 ユナイテッド・ユーティリティーズ・ピーエルシー Method and apparatus for aeration

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