JPS62213897A - Method and apparatus for aerating dam reservoir - Google Patents

Method and apparatus for aerating dam reservoir

Info

Publication number
JPS62213897A
JPS62213897A JP61054354A JP5435486A JPS62213897A JP S62213897 A JPS62213897 A JP S62213897A JP 61054354 A JP61054354 A JP 61054354A JP 5435486 A JP5435486 A JP 5435486A JP S62213897 A JPS62213897 A JP S62213897A
Authority
JP
Japan
Prior art keywords
water
air
aeration
bubble column
dam reservoir
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
JP61054354A
Other languages
Japanese (ja)
Inventor
Ichiro Minoshima
蓑島 一郎
Hisashi Wakamatsu
久 若松
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.)
JIYABARA KK
Original Assignee
JIYABARA KK
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 JIYABARA KK filed Critical JIYABARA KK
Priority to JP61054354A priority Critical patent/JPS62213897A/en
Publication of JPS62213897A publication Critical patent/JPS62213897A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20Mixing gases with liquids
    • B01F23/23Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/231Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids by bubbling
    • B01F23/23105Arrangement or manipulation of the gas bubbling devices
    • B01F23/2311Mounting the bubbling devices or the diffusers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20Mixing gases with liquids
    • B01F23/23Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/231Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids by bubbling
    • B01F23/23105Arrangement or manipulation of the gas bubbling devices
    • B01F23/2311Mounting the bubbling devices or the diffusers
    • B01F23/23115Mounting the bubbling devices or the diffusers characterised by the way in which the bubbling devices are mounted within the receptacle
    • B01F23/231154Mounting the bubbling devices or the diffusers characterised by the way in which the bubbling devices are mounted within the receptacle the bubbling devices being provided with ballast to keep them floating under the surface, i.e. when the bubbling devices are lighter than the liquid
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20Mixing gases with liquids
    • B01F23/23Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/232Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles
    • B01F23/2323Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles by circulating the flow in guiding constructions or conduits
    • B01F23/23231Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles by circulating the flow in guiding constructions or conduits being at least partially immersed in the liquid, e.g. in a closed circuit
    • B01F23/232311Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles by circulating the flow in guiding constructions or conduits being at least partially immersed in the liquid, e.g. in a closed circuit the conduits being vertical draft pipes with a lower intake end and an upper exit end
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/30Driving arrangements; Transmissions; Couplings; Brakes
    • B01F35/32Driving arrangements
    • B01F35/32005Type of drive
    • B01F35/3203Gas driven
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/30Driving arrangements; Transmissions; Couplings; Brakes
    • B01F35/32Driving arrangements
    • B01F35/32005Type of drive
    • B01F35/32015Flow driven

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)

Abstract

PURPOSE:To contrive to improve water quality, by forming a water lifting flow passage in a water area and sending air bubbles of compressed air into said flow passage from a lower area to dissolve and mix oxygen as much as possible. CONSTITUTION:An air bubble generator 2 of compressed air is arranged inside the lower part of a cylindrical air bubble tower 1a having a water introducing port 1a opened to a deep water layer at the lower end part thereof and a water introducing port 1b at the upper end part thereof. Compressed air is supplied to the air bubble generator 2 from a compressor C through a transfer hose T to generate and supply air bubbles. The length of the tower 1a is regulated corresponding to the depth of water to regulate the amount of air and an air bubble rising speed corresponding to the capacity of a water area and the compressor C is operated to send compressed air to the air bubble generator 2. Generated air bubbles have a fast rising speed and oxygen is sufficiently dissolved-in and mixed with the water present in the tower to enhance DO-concn. By this method, effective aeration is performed.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 この発明はダム貯水池や湖沼等の水質保全対策として用
いられる曝気方法及びその装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to an aeration method and apparatus for use as a water quality conservation measure in dam reservoirs, lakes, etc.

周知のごとくダム貯水池等は、気温が上昇する春期から
夏期にかけては、自然に対流循環を起す秋期ないし冬期
とは異なり、第1図に示すごとく水域が表水層E、変水
層M、深水層Hと成層固定され、水域全体に渡る自然の
対流循環が生起しない。従ってこの時期における深水層
ト1の水は、表水層Eの水と混合しなくなる等の理由か
ら、溶存酸素(Do>11度は著しく低下し、場合によ
ってはゼロ状態にまで進行し、水底から栄養塩の流出や
有害物の溶出が惹起するきわめて好ましからざる事態に
至る。
As is well known, in dam reservoirs, etc., from spring to summer when the temperature rises, unlike in autumn and winter when convective circulation occurs naturally, the water area is divided into surface layer E, variable layer M, and deep water as shown in Figure 1. The stratification is fixed with layer H, and natural convective circulation throughout the water body does not occur. Therefore, during this period, the water in the deep water layer T1 no longer mixes with the water in the surface water layer E, and dissolved oxygen (Do > 11 degrees) decreases significantly, and in some cases progresses to zero, and the water at the bottom of the water. This leads to extremely undesirable situations such as the outflow of nutrients and the elution of harmful substances.

〔従来の技術〕[Conventional technology]

そこで従来からこの種の水質保全対策の−として全層曝
気装置が提供されてきた。例えば水底域に気泡発生装置
を設け、陸上のコンプレッサーから供給される空気を直
接噴出させて深水層の水のDO1度を増大させようとす
るものである。この装置では通常は、水に対し、できる
限り空気の溶解をし易くするために、水との接触面積を
大きくするべく可及的に小径の気泡を発生させるように
している。
Therefore, full-layer aeration devices have been provided as a water quality conservation measure of this type. For example, a bubble generator is installed in the underwater area, and air supplied from a land-based compressor is directly blown out to increase the DO1 degree of water in the deep water layer. This device usually generates air bubbles as small as possible in order to increase the contact area with water in order to facilitate the dissolution of air into water as much as possible.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

しかしながら一方で、気泡はある一定の大きさ以下の小
径の気泡では、その上昇速度が遅いためダム貯水池管の
大容量の水域全体を強制的に対流するまでには至らず、
局部的な酸素供給に止まり、本質的な水質改善を図るも
のではなく、著しく問題の有するところであった。
However, on the other hand, bubbles with small diameters below a certain size have a slow rate of rise, so they are not able to force convection throughout the large volume of water in the dam reservoir pipe.
This method was limited to local oxygen supply, did not substantially improve water quality, and was extremely problematic.

この点で特公昭42−25987M公報所載の発明に係
る曝気装置は、管内に空気だめを設けて、ある一定量以
上の空気がたまると、その空気塊が一気に管内を上昇す
ることによってサイホン作用を起し、これにより水底の
水塊を管内に吸い込ませるとともに、一方で吹き上げ、
水面にまで揚水して当該水面上で水平方向に拡散させ、
もって対流系を形成するというもので、いわば間欠式曝
気装置とした点において前記装置の欠点を解消したもの
といえる。
In this respect, the aeration device according to the invention disclosed in Japanese Patent Publication No. 42-25987M provides an air reservoir in the pipe, and when a certain amount of air accumulates, the air mass rises inside the pipe at once, causing a siphon effect. This causes the water mass at the bottom to be sucked into the pipe, while also blowing it up.
Pump water up to the water surface and spread it horizontally on the water surface,
This forms a convection system, and can be said to be an intermittent aeration system that overcomes the drawbacks of the previous systems.

しかしながらこの装置は、どちらかといえば水に対して
直接、酸素を溶解させて供給する働きにおいてはきわめ
て乏しく、むしろ強制的な対流循環のみを生起させて、
水域の混合を起し、もって成層を破壊して酸素を供給す
る方法を採るため、貯水池等の水域全体のDO濃度を高
めるには著しく時間を要するという難点があった。しか
もこの装置では、深水層の水を強制的に表水層等に混合
させることから、一旦成層が固定され、深水−のDOI
度が低くもしくはゼロ状態となった後においては、表水
層の水質障害を確実に招来することになってすこぶる好
ましくなかった。
However, this device is extremely poor at dissolving and supplying oxygen directly to water; rather, it only causes forced convective circulation.
Since this method involves mixing water bodies, thereby destroying the stratification and supplying oxygen, there is a problem in that it takes a considerable amount of time to increase the DO concentration in the entire body of water such as a reservoir. Moreover, since this device forcibly mixes the water in the deep water layer with the surface water layer, the stratification is fixed and the DOI of the deep water layer is fixed.
After the water level reaches a low or zero level, water quality in the surface water layer will definitely be impaired, which is extremely undesirable.

そこでこの発明の目的とするところは、上述の問題点を
悉く解決しようとしたもので、DOI度が低くもしくは
ゼロ状態にある深水層の水に対して、ダイレクトに酸素
を供給して即時的もしくは局部的に0Ofa度を高める
ことができ、しかも、所定の水域全体を均一混合し得る
に足る強制的な対流循環をも同時に生起させ、水域全体
において飛躍的な001度の向上を図ることができる曝
気方法及びその装置を提供しようとするところにある。
Therefore, the purpose of this invention is to solve all of the above-mentioned problems by directly supplying oxygen to water in the deep water layer where the DOI level is low or zero. It is possible to locally increase the 0Ofa degree, and at the same time generate forced convection circulation sufficient to uniformly mix the entire predetermined water area, thereby dramatically improving the 001 degree temperature in the entire water body. The present invention is intended to provide an aeration method and apparatus.

〔問題点を解決するための手段〕[Means for solving problems]

上記目的達成のためこの発明は、所定の水域内において
、垂直方向に比較的長く、かつ限られた−電空間を有す
る揚水流路を構成し、この揚水流路に、下方域から、流
路全体に可及的に分散充満し得る比較的直径の小さい圧
縮空気の気泡を送り込み、この揚水流路において、酸素
を可及的に溶解混合させるとともに、上昇する気泡の浮
揚力と、水塊の軽比重化に伴う浮力とにより、流路上方
域に向う上昇流を発生せしめ、水を揚水流路を通して下
方域から上方域へ連続的に送給するとともに、上方域に
おいて強制的に水平方向に拡散させ、所定の水域内金体
を強制循環対流させて、水域全体の溶存酸素濃度を高め
るようにしたことを特徴とするダム貯水池等の曝気方法
を採用した。またざらにこの発明は当該方法発明を実施
するにあたって、下方部に、深水層に開口する水の導入
口を有し、上方部に導出口を有する比較的管長の長い筒
状気泡塔と、この筒状気泡塔の下方部内側もしくはその
近傍位置に配設され、塔内存在の水に対して比較的直径
の小さい気泡を発生・供給する圧縮気体の気泡発生装置
とを有し、筒状気泡塔内部において、分散状態で上昇す
るこの気泡により、当該水に酸素を可及的に溶解混合さ
せるとともに同時に気泡塔上方部に向う上昇水流を生起
させ、気泡塔上方部には、この上昇流で前記導出口より
流出する溶存酸素濃度の高い水を、円周方向に水平に強
制拡散させるインペラーを設けたことを特徴とするダム
貯水池等の曝気装置を採用した。
In order to achieve the above object, the present invention constructs a pumping channel that is relatively long in the vertical direction and has a limited electric space in a predetermined water body, and connects the pumping channel from the lower area to the pumping channel. Compressed air bubbles with a relatively small diameter that can be dispersed and filled as much as possible are sent in, and in this pumping flow path, oxygen is dissolved and mixed as much as possible, and the buoyancy of the rising bubbles and the water mass are The buoyancy caused by the reduction in specific gravity generates an upward flow toward the upper region of the channel, and the water is continuously fed from the lower region to the upper region through the pumping channel, and is forced horizontally in the upper region. We adopted an aeration method for dams and reservoirs that is characterized by diffusion and forced circulation convection of metal bodies within a predetermined water area to increase the dissolved oxygen concentration in the entire water area. Furthermore, in carrying out the method invention, this invention includes a relatively long cylindrical bubble column having a water inlet opening into the deep water layer in the lower part and an outlet in the upper part; A compressed gas bubble generator is disposed inside or near the lower part of the cylindrical bubble column, and generates and supplies bubbles with a relatively small diameter to the water present in the column. Inside the tower, these bubbles rising in a dispersed state dissolve and mix oxygen into the water as much as possible, and at the same time generate an upward water flow toward the upper part of the bubble tower. An aeration device for a dam reservoir or the like is used, which is equipped with an impeller that forcibly diffuses water with a high dissolved oxygen concentration flowing out from the outlet in a circumferential direction and horizontally.

〔作用〕[Effect]

この発明は上述の様な構成を採用したことにより、深水
層の水は、比較的小径の気泡たる圧縮気体の溶解によっ
て局部的、即時的にDo濃度を向上させると同時に、揚
水流路たる気泡塔内において気泡の上昇に伴って当該水
塊は拡散状態で上昇し、この上昇流で揚水流路から外部
に流出し、ざらにインペラー等の強制拡散手段によって
円周方向に水平に拡散される。これによりDo濃度の乏
しいもしくはゼロ状態の深水層の水に対し直接水質改善
を図ると同時に、所定の水域全体の強制的な対流循環に
よってDO濃度の改善が図られる。
By adopting the above-mentioned configuration, this invention improves the Do concentration locally and instantly by dissolving the compressed gas in the form of relatively small-diameter air bubbles in the water of the deep water layer, and at the same time, the air bubbles in the pumping flow path As the bubbles rise in the tower, the water mass rises in a diffused state, and this upward flow flows out from the pumping channel to the outside, where it is diffused horizontally in the circumferential direction by a forced diffusion means such as an impeller. . This not only directly improves the water quality of water in the deep water layer where the Do concentration is low or zero, but also improves the DO concentration through forced convective circulation throughout the predetermined water body.

なお特に所定水域を仝層水域とした場合は、D。In particular, if the designated water area is a sub-layer water area, D.

濃度の高い表水層の水塊をも深水層にまで送り込むこと
になり、相乗的にDo濃度は高められる。
The water mass in the surface water layer with high concentration is also sent to the deep water layer, and the Do concentration is increased synergistically.

また所定水域を深水層にのみ限れば、変水層を全く破壊
せずして適切な曝気を行うことができる。
Furthermore, if the predetermined water area is limited to the deep water layer, appropriate aeration can be performed without destroying the variable water layer at all.

〔実施例〕〔Example〕

第1図はこの発明に係る方法を実施する際に用いる曝気
装置の一実施例を示1概略図であり、仝層曝気に適用し
た場合の使用状態を示している。
FIG. 1 is a schematic diagram showing an embodiment of an aeration apparatus used in carrying out the method according to the present invention, and shows the state of use when sublayer aeration is applied.

すなわち、1は下端部に、深水層Hに開口する水塊の導
入口1aを有し、上端部に水塊の導出口1bを有する比
較的管長の長い筒状気泡塔であり、この筒状気泡塔1の
下部内側に圧縮気体の気泡発生装置2が配設されている
。この気泡発生装置2は、塔内存在の水塊に対し比較的
直径の小さな気泡を発生・供給するもので、その圧縮気
体は地上に設置されたコンプレッサーCから移送ホース
Tを介して送給されている。一方、3はこの筒状気泡塔
の上部に設けられたフロートであり、筒状気泡塔下方部
に取り付けられたアンカー4との浮力バランスによって
水域内において垂直状態に固定されている。また5は気
泡塔上方部に設けられたインペラーであり、気泡塔内部
を拡散状態で上昇する水塊の上昇流によって自然に回動
するようになっている。なお6はインペラー5の回転軸
の軸受である。
That is, 1 is a relatively long cylindrical bubble column having a water mass inlet 1a opening into the deep water layer H at the lower end and a water mass outlet 1b at the upper end. A compressed gas bubble generator 2 is disposed inside the lower part of the bubble column 1. This bubble generator 2 generates and supplies bubbles with a relatively small diameter to the water mass existing in the tower, and the compressed gas is sent from a compressor C installed on the ground via a transfer hose T. ing. On the other hand, 3 is a float provided on the upper part of this cylindrical bubble column, and is fixed vertically in the water body by the buoyancy balance with the anchor 4 attached to the lower part of the cylindrical bubble column. Further, reference numeral 5 denotes an impeller provided in the upper part of the bubble column, and is designed to rotate naturally by the upward flow of the water mass that rises in a diffused state inside the bubble column. Note that 6 is a bearing for the rotating shaft of the impeller 5.

またこの実施例では、筒状気泡塔2が上下方向に伸縮可
能な伸縮管として構成されており、伸縮手段としてはジ
ャバラ構造体7を気泡塔中間部に配設している。
Further, in this embodiment, the cylindrical bubble column 2 is configured as an expandable tube that can be expanded and contracted in the vertical direction, and a bellows structure 7 is disposed in the middle part of the bubble column as an expansion and contraction means.

従ってこの曝気装置を全層曝気に使用するにあたっては
、まず水深に応じて管長を調節し、水域容量に応じて空
気量及び気泡上昇速度を調節して、次にコンプレッサー
Cを稼動させれば、圧縮気体たる圧縮空気が気泡発生装
置2内に送り込まれ、最適条件の気泡を発生させること
になる。この気泡は上昇速度が早く、かつ比較的直径の
小さい気泡であるため、塔内存在の水塊に充分酸素を溶
解混合供゛給してDo濃度が高められるとともに、上昇
する気泡の浮揚力により塔内占有の空気量の体積相当分
上昇しかつまた比重が塔外水塊に比して軽くなるために
、飛躍的な上昇流に発達する。この上昇流により、再び
導入口1aより新たなり。
Therefore, when using this aeration device for full-layer aeration, first adjust the pipe length according to the water depth, adjust the air volume and bubble rising speed according to the water area capacity, and then operate the compressor C. Compressed air, which is a compressed gas, is fed into the bubble generator 2 to generate bubbles under optimal conditions. Since these bubbles have a fast rising speed and a relatively small diameter, they can sufficiently dissolve and mix oxygen into the water mass existing in the tower, increasing the Do concentration, and due to the buoyancy force of the rising bubbles. Since the amount of air occupied inside the tower rises by an amount equivalent to the volume, and the specific gravity becomes lighter than that of the water mass outside the tower, a dramatic upward flow develops. Due to this upward flow, fresh air flows from the inlet 1a again.

濃度の乏しい深水層ト1の水が導入される一方で、導出
口1bよりDo濃度の高い水が塔外に放出される。放出
された当該水は、回動するインペラー5によって円周方
向に水平に著しく強制拡散される。従ってこれらの水の
流れによって深水層ト1から表水層Eに至る水域全体に
対流系が生じ、水の循環が行われるものとなる。
Water with a low concentration in the deep water layer 1 is introduced, while water with a high Do concentration is discharged to the outside of the tower from the outlet 1b. The discharged water is forcefully dispersed horizontally in the circumferential direction by the rotating impeller 5. Therefore, due to these water flows, a convection system is generated throughout the water area from the deep water layer T1 to the surface water layer E, and water circulation is performed.

ところでこの実施例では、水深に応じて、さらには後述
する深水層曝気式との兼用タイプとするために、管長を
調節するべく筒状気泡塔を伸縮管で構成しているが、も
ち論これに限定されるものではない。その貯水池等の水
深等に応じて管長を一定にしても差し支えない。またこ
の実施例ではインペラー5の回転力は塔内を上昇する水
流によって与えられており、いわば自然回動のみによっ
て拡散作用を発揮させているが、もち論モーター駆動等
の強制駆動手段によって回動させてもよいのはもち論で
ある。水域の大きさ等に応じて適宜採用すればよい。ま
た、装置全体の固定手段もフロート式を採用したこの実
施例に限られるものでは熱論なく、従来より採用されて
きた各種の手段を適宜採用すれば差し支えない。
By the way, in this embodiment, the cylindrical bubble column is constructed with an expandable tube in order to adjust the tube length according to the water depth and also to be compatible with the deep water layer aeration type described later. It is not limited to. There is no problem in keeping the length of the pipe constant depending on the water depth of the reservoir, etc. Furthermore, in this embodiment, the rotational force of the impeller 5 is given by the water flow rising inside the tower, and the diffusion effect is exerted only by natural rotation, so to speak. It is only natural that it is okay to do so. It may be adopted as appropriate depending on the size of the water area, etc. Further, the means for fixing the entire apparatus is not limited to this embodiment which employs a float type, and various conventionally employed means may be used as appropriate.

ところでこの実施例に係る曝気装置は仝層曝気のみなら
ず、深水層曝気に対しても適用することができる。すな
わち第2図に示すごとく、深水層Hの層厚に応じて管長
を調節すれば適用し1qるものである。特に深水層曝気
の場合、全層曝気への適用に比して管長は短くなること
からその短かさに応じて塔内に生じる上昇流は減少する
ことになるほか、インペラー5によっても水平方向に拡
散された気泡は分散するため、表水層Eはもち論、変水
層Mをも破壊せずして深水層のみを対客としてダイ゛レ
クトに酸素供給することができると同時に、適度な対流
循環を起し、きわめて迅速に深水層曝気を行い得る。な
おこの種の曝気の場合においても、管長のほか管径や、
気泡発生装置から発生する気泡径ないし空気伍あるいは
気泡上昇速度を適宜調節することにより最適条件下で深
層曝気がなされるものである。
By the way, the aeration device according to this embodiment can be applied not only to low-layer aeration but also to deep-water layer aeration. That is, as shown in FIG. 2, if the pipe length is adjusted according to the thickness of the deep water layer H, the length of the pipe can be reduced by 1q. In particular, in the case of deep-water layer aeration, the pipe length is shorter than in full-layer aeration, so the upward flow generated within the tower is reduced accordingly, and the impeller 5 also reduces the horizontal flow. Since the diffused air bubbles are dispersed, it is possible to directly supply oxygen to only the deep water layer without destroying not only the surface water layer E but also the variable water layer M. Convection circulation occurs and deep water layer aeration can be carried out extremely quickly. In addition, in the case of this type of aeration, in addition to the pipe length, the pipe diameter,
Deep aeration is carried out under optimal conditions by appropriately adjusting the bubble diameter, air size, or bubble rising speed generated from the bubble generator.

従って既述した曝気メカニズムを採用すれば、深水層の
みを対象とする曝気装置の採用も充分可能である。
Therefore, by employing the aeration mechanism described above, it is fully possible to employ an aeration device that targets only the deep water layer.

〔発明の効果〕〔Effect of the invention〕

以上のごとくこの発明は、DO濃度が少なくもしくはゼ
ロ状態にある深水層の水塊に対してダイレクトに圧縮気
体を供給溶解させて即時的もしくは局部的にDO濃度を
高める機能と、所定の水域全体を均一混合し得るに足る
強制的な対流循環をも生起させる機能とを同時に並備す
るために、水域全体において相乗的にしかもきわめて短
期間でDO濃度が高められる効果を発揮し得るに至った
As described above, this invention provides a function to directly or locally increase the DO concentration by supplying and dissolving compressed gas directly to the water mass in the deep water layer where the DO concentration is low or zero, and Because it simultaneously has the function of generating forced convective circulation sufficient to uniformly mix the DO, it has become possible to exhibit the effect of increasing the DO concentration synergistically and in an extremely short period of time throughout the entire water body. .

従って従来から全層曝気タイプにおいて固有の問題であ
った深水層の水塊に対する処理時間と処理量は同時に良
好に満足することとなり、従来のごとくDOm度の低い
もしくはゼロ状態の深水層を表水層に揚水して表水層の
水質悪化を招来することは全くなく、しかも底面での栄
養塩の蓄積を抑制等することができ、きわめて効果的な
曝気を行い1qるものである。また一方、深水層曝気と
じても応用できるものであり、当該技術分野に資すると
ころきわめて大ぎな曝気方法及びその装置を提供し得た
のである。
Therefore, the processing time and processing amount for the water mass in the deep water layer, which had been a problem unique to the conventional full-layer aeration type, are both satisfactorily satisfied at the same time. It does not cause any deterioration of water quality in the surface water layer by pumping water into the layer, and it also suppresses the accumulation of nutrients at the bottom, and provides extremely effective aeration. On the other hand, it can also be applied to deep water layer aeration, and has provided an extremely significant aeration method and apparatus that will contribute to this technical field.

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

第1図はこの発明に係る曝気装置の一実施例において、
仝層曝気に適用した場合の使用状態を示す概略図、 第2図は同実施例において、深層曝気に適用した場合の
使用状態を示す概略図である。
FIG. 1 shows an embodiment of the aeration device according to the present invention.
FIG. 2 is a schematic diagram showing a usage state when deep aeration is applied in the same embodiment. FIG. 2 is a schematic diagram showing a usage state when deep aeration is applied in the same embodiment.

Claims (9)

【特許請求の範囲】[Claims] (1)所定の水域内において、垂直方向に比較的長く、
かつ限られた一定空間を有する揚水流路を構成し、この
揚水流路に、下方域から、流路全体に可及的に分散充満
し得る比較的直径の小さい圧縮空気の気泡を送り込み、
この揚水流路において、酸素を可及的に溶解混合させる
とともに、上昇する気泡の浮揚力と、水塊の軽比重化に
伴う浮力とにより、流路上方域に向う上昇流を発生せし
め、水を揚水流路を通して下方域から上方域へ連続的に
送給するとともに、上方域において強制的に水平方向に
拡散させ、所定の水域内全体を強制循環対流させて、水
域全体の溶存酸素濃度を高めるようにしたことを特徴と
するダム貯水池等の曝気方法。
(1) relatively long in the vertical direction within a given body of water;
and constructing a pumping channel having a limited fixed space, and feeding compressed air bubbles with a relatively small diameter into the pumping channel from a lower region so as to be able to disperse and fill the entire channel as much as possible,
In this pumping channel, oxygen is dissolved and mixed as much as possible, and the buoyant force of the rising bubbles and the buoyant force accompanying the light specific gravity of the water mass generate an upward flow toward the upper region of the channel, and the water is continuously delivered from the lower region to the upper region through the pumping channel, and is forcibly diffused horizontally in the upper region, causing forced circulation convection throughout the entire predetermined water area, and reducing the dissolved oxygen concentration in the entire water area. A method for aerating a dam reservoir, etc., characterized in that the aeration is increased.
(2)揚水流路が変水層を越えて比較的長く、かつ限ら
れた一定空間を有する特許請求の範囲第1項記載のダム
貯水池等の曝気方法。
(2) The method for aerating a dam reservoir, etc., according to claim 1, wherein the pumping channel is relatively long beyond the variable water layer and has a limited fixed space.
(3)湯水流路が変水層を越えない範囲において比較的
長く、かつ限られた一定空間を有する特許請求の範囲第
1項記載の曝気方法。
(3) The aeration method according to claim 1, wherein the hot water flow path is relatively long and has a limited fixed space within a range that does not exceed the variable water layer.
(4)下方部に、深水層に開口する水の導入口を有し、
上方部に導出口を有する比較的管長の長い筒状気泡塔と
、この筒状気泡塔の下方部内側もしくはその近傍位置に
配設され、塔内存在の水に対して比較的直径の小さい気
泡を発生・供給する圧縮気体の気泡発生装置とを有し、
筒状気泡塔内部において、分散状態で上昇するこの気泡
により、当該水に酸素を可及的に溶解混合させるととも
に同時に気泡塔上方部に向う上昇水流を生起させ、気泡
塔上方部には、この上昇流で前記導出口より流出する溶
存酸素濃度の高い水を、円周方向に水平に強制拡散させ
るインペラーを設けたことを特徴とするダム貯水池等の
曝気装置。
(4) Has a water inlet opening into the deep water layer in the lower part,
A cylindrical bubble column with a relatively long tube length and an outlet in the upper part, and bubbles that are arranged inside or near the lower part of the cylindrical bubble column and have a relatively small diameter relative to the water present in the column. It has a compressed gas bubble generator that generates and supplies
Inside the cylindrical bubble column, these bubbles rising in a dispersed state dissolve and mix oxygen into the water as much as possible, and at the same time generate an upward water flow toward the upper part of the bubble column. An aeration device for a dam reservoir, etc., characterized in that it is provided with an impeller that horizontally and forcefully diffuses water with a high dissolved oxygen concentration flowing out from the outlet in an upward flow in a circumferential direction.
(5)筒状気泡塔が、変水層を越える比較的長い管長を
有する特許請求の範囲第4項記載のダム貯水池等の曝気
装置。
(5) The aeration device for a dam reservoir or the like according to claim 4, wherein the cylindrical bubble column has a relatively long pipe length that extends beyond the variable water layer.
(6)筒状気泡塔が、変水層を越えない程度の比較的長
い管長を有する特許請求の範囲第4項記載のダム貯水池
等の曝気装置。
(6) The aeration device for a dam reservoir or the like according to claim 4, wherein the cylindrical bubble column has a relatively long pipe length that does not exceed the variable water layer.
(7)筒状気泡塔が、上下方向に伸縮可能な伸縮管であ
る特許請求の範囲第4項記載のダム貯水池等の曝気装置
(7) The aeration device for a dam reservoir or the like according to claim 4, wherein the cylindrical bubble column is an expandable tube that can be expanded and contracted in the vertical direction.
(8)インペラーを上昇水流で回動する特許請求の範囲
第4項、第5項、第6項または第7項記載のダム貯水池
等の曝気装置。
(8) An aeration device for a dam reservoir or the like according to claim 4, 5, 6, or 7, in which the impeller is rotated by a rising water flow.
(9)インペラーをモーター駆動により強制回動する特
許請求の範囲第4項、第5項、第6項または第7項記載
のダム貯水池等の曝気装置。
(9) An aeration device for a dam reservoir or the like according to claim 4, 5, 6, or 7, in which the impeller is forcibly rotated by motor drive.
JP61054354A 1986-03-12 1986-03-12 Method and apparatus for aerating dam reservoir Pending JPS62213897A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61054354A JPS62213897A (en) 1986-03-12 1986-03-12 Method and apparatus for aerating dam reservoir

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61054354A JPS62213897A (en) 1986-03-12 1986-03-12 Method and apparatus for aerating dam reservoir

Publications (1)

Publication Number Publication Date
JPS62213897A true JPS62213897A (en) 1987-09-19

Family

ID=12968296

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61054354A Pending JPS62213897A (en) 1986-03-12 1986-03-12 Method and apparatus for aerating dam reservoir

Country Status (1)

Country Link
JP (1) JPS62213897A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0470198U (en) * 1990-10-23 1992-06-22
WO2008035860A1 (en) * 2006-09-20 2008-03-27 Kui-Yeun Kim The high efficiency aerator apparatus
US7571899B2 (en) * 2004-02-03 2009-08-11 Matsuedoken Co., Ltd. Gas-liquid dissolving apparatus
JP2009207971A (en) * 2008-03-03 2009-09-17 Marsima Aqua System Corp Air lift device
JP2012528714A (en) * 2009-09-15 2012-11-15 エココ カンパニー リミテッド Green algae-preventing water circulation system using sunlight
JPWO2015008788A1 (en) * 2013-07-18 2017-03-02 株式会社エコ・プラン Vertical circulation method and vertical circulation device for closed water area

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5015957B1 (en) * 1969-10-07 1975-06-09
JPS5316860U (en) * 1976-07-23 1978-02-13

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5015957B1 (en) * 1969-10-07 1975-06-09
JPS5316860U (en) * 1976-07-23 1978-02-13

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0470198U (en) * 1990-10-23 1992-06-22
US7571899B2 (en) * 2004-02-03 2009-08-11 Matsuedoken Co., Ltd. Gas-liquid dissolving apparatus
WO2008035860A1 (en) * 2006-09-20 2008-03-27 Kui-Yeun Kim The high efficiency aerator apparatus
JP2009207971A (en) * 2008-03-03 2009-09-17 Marsima Aqua System Corp Air lift device
JP2012528714A (en) * 2009-09-15 2012-11-15 エココ カンパニー リミテッド Green algae-preventing water circulation system using sunlight
JPWO2015008788A1 (en) * 2013-07-18 2017-03-02 株式会社エコ・プラン Vertical circulation method and vertical circulation device for closed water area

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