JPH05146236A - Apparatus for raising aquatic organism - Google Patents

Apparatus for raising aquatic organism

Info

Publication number
JPH05146236A
JPH05146236A JP3335915A JP33591591A JPH05146236A JP H05146236 A JPH05146236 A JP H05146236A JP 3335915 A JP3335915 A JP 3335915A JP 33591591 A JP33591591 A JP 33591591A JP H05146236 A JPH05146236 A JP H05146236A
Authority
JP
Japan
Prior art keywords
growing
cylindrical body
water
bubbles
aerator
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
JP3335915A
Other languages
Japanese (ja)
Other versions
JP3127536B2 (en
Inventor
Hirobumi Onari
博文 大成
Mitsuo Morimoto
光雄 森元
Katsutoshi Watanabe
勝利 渡邊
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.)
OSHIMA KOKI KK
Original Assignee
OSHIMA KOKI 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 OSHIMA KOKI KK filed Critical OSHIMA KOKI KK
Priority to JP03335915A priority Critical patent/JP3127536B2/en
Publication of JPH05146236A publication Critical patent/JPH05146236A/en
Application granted granted Critical
Publication of JP3127536B2 publication Critical patent/JP3127536B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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
    • B01F23/232Mixing 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Farming Of Fish And Shellfish (AREA)

Abstract

PURPOSE:To increase the amount of dissolved oxygen in water used for raising aquatic organisms by vertically installing a turning type aerator equipped with an air inlet under a lower opening of a cylindrical unit having helical plates fixed on the inner wall. CONSTITUTION:Air is released from an air inlet 66 under a cylindrical unit 60 having helical plates 61 fixed on the inner wall into water for raising. The air is finely divided by turning in the cylinder and its lifting speed is increased in a gradually constricted cylindrical unit 60' to feed fine bubbles into the tank for raising aquatic organisms.

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、魚類、貝類等の水生動
物あるいは昆布、若布等の水生植物等の育成装置に関
し、特に育成用水に微細な酸化ガス、炭酸ガス等の気泡
を供給し、かつ育成用水内に強力な安定した循環流を形
成し得るエアレータを備えた水生生物育成装置に関する
ものである。
FIELD OF THE INVENTION The present invention relates to an apparatus for growing aquatic animals such as fish and shellfish or aquatic plants such as kelp and young cloth, and particularly supplies fine bubbles of oxidizing gas, carbon dioxide gas, etc. to the growing water, In addition, the present invention relates to an aquatic organism growing device including an aerator capable of forming a strong and stable circulating flow in the growing water.

【0002】[0002]

【従来の技術及び発明が解決しようとする課題】従来、
水生生物育成装置におけるエアレーションには、育成槽
内に設置された環状や板状のエアレータ細孔から空気を
育成用水中に加圧して噴き出すことによって気泡を細分
化する方式と回転羽根や気泡噴流などによりせん断力が
形成された育成用水流内に空気を入れてそれを細分化す
る方式がある。
2. Description of the Related Art Conventionally, the problems to be solved by the invention
For aeration in aquatic organism growing equipment, a method of subdividing bubbles by pressurizing and ejecting air into the growing water from the annular or plate-shaped aerator pores installed in the growing tank, rotary blades, bubble jets, etc. There is a method in which air is introduced into the growing water flow in which the shearing force has been formed by subdividing it.

【0003】そして、これら機能を有するエアレータに
よるエアレーションでは、基本的には空気の送給量やそ
れぞれのエアレータの設置個数等によって必要な調節が
行われている。しかし、省エネルギー型の高度水生生物
育成を目的とする高性能水生生物育成装置の開発のため
には、特に微細な酸化ガス気泡を多量に発生させ、さら
にはその気泡の発生量を制御する必要がある。
In aeration using an aerator having these functions, basically, necessary adjustments are made depending on the amount of air fed and the number of aerators installed. However, in order to develop a high-performance aquatic organism breeding apparatus for the purpose of energy-saving advanced aquatic organism breeding, it is necessary to generate a large amount of fine oxidizing gas bubbles and to control the amount of bubbles generated. is there.

【0004】ところが、上記の方式のエアレーションに
は、そのほとんどが噴き出しによる散気方式か回転羽根
や突起体とにせん断によって気泡を発生させる方式であ
るために、下記のさまざまな欠点があった。例えば、散
気管、散気板、散気筒からの噴き出し方式では、そこに
いかに微細な細孔を設けても、気泡が細孔から噴出する
際の気泡の表面張力によって、結果的に数mm程度の径
を有する大きな気泡が発生してしまい、それよりも小さ
な気泡を発生させることが不可能であるという欠点を有
していた。また、このような散気方式の欠点として、そ
の長時間運転に伴って発生する目づまり問題と動力費の
増大の問題等が存在していた。一方、回転羽根や気泡噴
流などによりせん断力が形成された育成用水流内に空気
をいれてそれを細分化する方式では、キャビテーション
を発生させるのに高速の回転数が要求され、その動力費
の問題やキャビテーション発生に伴って急激に進行する
羽根の腐食や振動問題があり、さらに、微細気泡の生成
が少ないという問題もあった。
However, most of the above-mentioned aeration methods are the air diffusion method by jetting or the method in which bubbles are generated by shearing on the rotary blades and the projections, so that they have the following various drawbacks. For example, in the ejection method from an air diffuser, an air diffuser, or a cylinder, no matter how fine pores are provided there, the surface tension of the bubbles when they eject from the pores results in about several mm. However, there is a drawback that large bubbles having a diameter of 10 are generated, and it is impossible to generate bubbles smaller than that. Further, as the drawbacks of such an air diffusion method, there are problems such as clogging that occurs during long-term operation and increase in power cost. On the other hand, in the method of subdividing air into the growing water flow in which a shearing force is formed by a rotating blade or a bubble jet, a high rotation speed is required to generate cavitation, and its power cost is reduced. There are problems such as blade corrosion and vibration that rapidly progress with the occurrence of cavitation, and there is also a problem that the generation of fine bubbles is small.

【0005】以上のような欠点や問題点を有した従来の
水生生物育成装置におけるエアレータにおいては、微細
気泡の生成量が少ないため気泡の育成用水中での滞留時
間が短くなり、育成用水中への酸素溶解量の増大が期待
できなかった。さらには、微細気泡の径と発生量を容易
に制御することができないことから、育成用水の調製が
効率的に実施できない問題があった。
In the aerator of the conventional apparatus for growing aquatic organisms having the above-mentioned drawbacks and problems, since the generation amount of fine bubbles is small, the residence time of the bubbles in the growing water is shortened, and the bubbles enter the growing water. The increase in the amount of dissolved oxygen could not be expected. Furthermore, since the diameter and amount of the fine bubbles cannot be easily controlled, there is a problem that the growth water cannot be efficiently prepared.

【0006】上術したようなエアレータの場合、次のよ
うな問題を有する。すなわち、 気泡の径が1mm以下で数10μm程度までの微細
気泡を大量にしかも均一に発生させることができず、気
液更新の飛躍的促進が達成できない。 上記のの気泡の径、分布、発生量を必要に応じて
機械的に容易に制御することができない。 気泡が吸い込まれた管内流れを適切に配備すること
によって、水生生物育成装置内に必要な循環流の形成や
撹拌作用をもたらすことができない。 回転羽根や突起に気液二相流が衝突する方式におい
ては、魚類や水生小生物が破壊されてしまい、水生生物
の育成に必要な環境の形成・維持に支障を来した。 連続散気により目づまりが発生し、散気効率が低下
することによって、圧力損失が増大する。このため長期
連続運転や運転経費の大幅な節減ができない。 気泡を供給するエアレータとコンプレッサーを含む
装置形状が大きく、設置上の制約が存在し、小型化が図
れない。 気泡の径、分布、発生量の制御によって、水生生物
育成槽内での撹拌や溶存酸素量の調整等による水生生物
育成の最適制御を行うことが困難である。
The aerator as described above has the following problems. That is, it is not possible to uniformly generate a large amount of fine bubbles having a diameter of 1 mm or less and up to about several tens of μm, and it is not possible to achieve a dramatic promotion of gas-liquid renewal. It is impossible to easily and mechanically control the diameter, distribution, and generation amount of the bubbles as described above. Appropriately arranging the in-pipe flow into which the air bubbles have been sucked cannot provide the necessary circulation flow formation and agitation action in the aquatic organism growing apparatus. In the method in which the gas-liquid two-phase flow collides with the rotating blades and protrusions, fish and aquatic small organisms are destroyed, which hinders the formation and maintenance of the environment necessary for aquatic organisms to grow. The continuous aeration causes clogging and reduces the aeration efficiency, which increases the pressure loss. Therefore, long-term continuous operation and significant reduction in operating costs cannot be achieved. The shape of the device, including the aerator that supplies air bubbles and the compressor, is large, and there are restrictions on the installation, so miniaturization cannot be achieved. It is difficult to perform optimal control of aquatic organism growth by agitation in the aquatic organism growth tank, adjustment of dissolved oxygen amount, and the like by controlling the diameter, distribution, and generation amount of bubbles.

【0007】[0007]

【課題を解決するための手段及び作用】本発明者らは上
記従来技術の問題点を解決すべく鋭意研究を重ねた結
果、育成用水に微細な気泡を容易に供給できる省エネ型
エアレータを備えた水生生物育成装置を開発した。すな
わち本発明は下記のとおりの水生生物育成装置である。
第1の発明は、内壁に螺旋板を固着してなる円筒体と該
円筒体下方開口部直下に若干の間隔をおいて配置された
空気供給口とから構成される旋回式エアレータを水生生
物育成槽内に垂設してなることを特徴とする水生生物育
成装置であり、第2の発明は、円筒体が、その全体又は
上方部が漸縮円筒体であることを特徴とする第1発明に
記載の水生生物育成装置であり、第3の発明は、螺旋板
が、多条のものであることを特徴とする第1発明又は第
2発明に記載の水生生物育成装置であり、第4の発明
は、円筒体内の中心軸に旋回板支持支柱を設けたことを
特徴とする第1ないし第3発明のいずれかに記載の水生
生物育成装置であり、第5の発明は、円筒体下方開口部
を縮小してなることを特徴とする第1ないし第4発明の
いずれかに記載の水生生物育成装置であり、そして、第
6の発明は、円筒体内壁に固着される螺旋板が、複数枚
であり、リード角が0.7〜1.3であることを特徴と
する第1ないし第5発明のいずれかに記載の水生生物育
成装置である。
Means and Actions for Solving the Problems As a result of intensive studies to solve the above-mentioned problems of the prior art, the present inventors have provided an energy-saving aerator capable of easily supplying fine bubbles to growing water. We developed aquatic organism breeding equipment. That is, the present invention is an aquatic organism growing apparatus as described below.
A first aspect of the present invention provides a swirling aerator, which comprises a cylindrical body having a spiral plate fixed to an inner wall thereof and an air supply port arranged at a slight interval immediately below the lower opening of the cylindrical body, to grow aquatic organisms. It is an aquatic organism growing device characterized by being hung vertically in a tank, and the second invention is the first invention, characterized in that the whole or upper part of the cylindrical body is a tapered cylinder. The aquatic organism growing apparatus according to the third aspect of the invention is the aquatic organism growing apparatus according to the first aspect or the second aspect of the invention, characterized in that the spiral plate is a multi-screw plate. The invention according to claim 1 is the aquatic organism growing apparatus according to any one of the first to third inventions, characterized in that a swivel plate support column is provided on the central axis of the cylindrical body, and the fifth invention is the lower cylindrical body. The water according to any one of the first to fourth inventions, characterized in that the opening is reduced. A sixth aspect of the present invention is a living organism growing apparatus, and the sixth invention is characterized in that a plurality of spiral plates are fixed to the inner wall of the cylindrical body, and the lead angle is 0.7 to 1.3. The aquatic organism growing apparatus according to any one of the fifth inventions.

【0008】以上の発明においては、第1に、本発明に
旋回方式によれば、従来の噴き出し方式のエアレータよ
りもかなり小さい圧力損失となり、育成用水の中への気
泡発生効率が飛躍的に向上する。第2に、従来の噴き出
し方式ではセラミックス製等の不規則多孔質管の細孔の
径をμm程度に小さくしてもそこから発生する気泡の径
は平均的に数mmほどあったが、本発明に係る旋回式の
エアレータによれば発生する微細気泡の平均径を数10
0μmから数10μmまでに微細化することができる。
よって、育成用水と酸化ガス気泡との接触面積を従来方
式の10〜100倍程度に高めることができ、さらに気
泡の滞留時間を10〜100倍に増長することができる
結果、水生生物育成用水中の溶解酸素量を飛躍的に増量
することができる。
In the above invention, firstly, according to the swirling method of the present invention, the pressure loss becomes much smaller than that of the conventional jet type aerator, and the efficiency of bubble generation in the growing water is dramatically improved. To do. Secondly, in the conventional jetting method, even if the diameter of the pores of the irregular porous tube made of ceramics or the like was reduced to about μm, the diameter of the bubbles generated therefrom was about several mm on average. According to the swirl type aerator of the present invention, the average diameter of the fine air bubbles generated is expressed in several tens.
The size can be reduced from 0 μm to several tens of μm.
Therefore, the contact area between the growing water and the oxidizing gas bubbles can be increased to about 10 to 100 times that of the conventional method, and the residence time of the bubbles can be increased to 10 to 100 times, resulting in the aquatic organism growing water. The amount of dissolved oxygen can be dramatically increased.

【0009】第3に、漸縮円筒体の採用により、上昇気
液二相流の流速が増強され、水槽内に強力かつ安定した
循環流を形成することができる。しかも、漸縮円筒体内
には格別な突起物が存在しないため、圧力損失はほとん
どない。また、旋回性の増大による流束縮小により、漸
縮円筒体内における圧力損失の影響はほとんどない。第
4に、高速回転羽根や突起体への衝突によつてエアレー
ションを行う従来の方式では、水生生物等が破壊される
問題があったが、本発明によればそうした問題はほとん
ど発生しない。第5に、円筒体下部開口部が縮小されて
いるものにあっては、気体の上昇に伴うエアリフト効果
をさらに向上させ、水槽底付近に沈澱する残渣等を巻き
上げ、水槽底付近の腐敗を防止する等、エアレーション
による浄化処理を一層増進することができる。第6に、
下方配置の空気供給管から噴き出された空気塊は、円筒
体中の上昇連行過程で微細化されるのでエアレータに目
づまりはほとんど発生しない。
Thirdly, by adopting the taper cylinder, the flow velocity of the rising gas-liquid two-phase flow is enhanced, and a strong and stable circulating flow can be formed in the water tank. Moreover, since there is no particular protrusion in the tapered cylinder, there is almost no pressure loss. Further, due to the reduction of the flux due to the increase of the swirling property, there is almost no influence of the pressure loss in the gradually contracting cylindrical body. Fourthly, in the conventional method in which aeration is performed by the collision with the high-speed rotating blade or the protrusion, there is a problem that aquatic organisms are destroyed, but according to the present invention, such a problem hardly occurs. Fifth, in the case where the lower opening of the cylindrical body is reduced, the airlift effect due to the rise of gas is further improved, and the residue and the like that settle near the bottom of the water tank are rolled up, and the decay near the bottom of the water tank is prevented. Therefore, the purification process by aeration can be further improved. Sixth,
The air mass ejected from the air supply pipe arranged below is atomized in the ascending and entraining process in the cylindrical body, so that the aerator is hardly clogged.

【0010】[0010]

【 実 施 例 】以下に、本発明の実施例のいくつかを図
面に基づいて説明する。図1は、本発明に係る旋回式エ
アレータを備えた水生生物育成装置の全体構成説明図を
示す。図中、2は水生生物育成水槽、21は育成水槽排
水取出口、22は排水導出管、3はブロワーもしくはコ
ンプレッサー、5は育成水槽排水浄化装置、51は濾過
布、52は濾過砂、6は旋回式エアレータ、65は水生
生物育成用気体を移送する気体移送管、V、Vはバ
ルブ、4は送水ポンプである。本実施例装置において
は、育成用気体移送管65の端部から、水槽2底部の育
成用水1中に垂設された旋回式エアレータ6へ育成用気
体が供給され、育成用水1中の溶存酸素量が大いに高め
られ、さらにその供給によって育成用水1内に循環流が
形成される。
EXAMPLES Some examples of the present invention will be described below with reference to the drawings. FIG. 1 is an overall configuration explanatory diagram of an aquatic organism growing apparatus including a swirl type aerator according to the present invention. In the figure, 2 is an aquatic organism growing water tank, 21 is a growing water tank drainage outlet, 22 is a drainage outlet pipe, 3 is a blower or compressor, 5 is a growing water tank drainage purification device, 51 is a filter cloth, 52 is filtered sand, and 6 is A swirl type aerator, 65 is a gas transfer pipe for transferring aquatic organism growing gas, V 1 and V 2 are valves, and 4 is a water pump. In the apparatus of the present embodiment, the growth gas is supplied from the end of the growth gas transfer pipe 65 to the swirl type aerator 6 vertically provided in the growth water 1 at the bottom of the water tank 2 to dissolve the dissolved oxygen in the growth water 1. The amount is greatly increased, and the supply thereof forms a circulating flow in the growing water 1.

【0011】育成槽2内においては水生生物からの排出
物が浮上するので、該排出物を含む排水を育成槽排水取
出口21より排水導出管22を介して取り出し、育成槽
排水浄化装置5へと導入する。育成槽排水浄化装置5
は、中間壁の濾過布51と濾過砂52によって左右に二
槽に分けられており、右槽に導入された排水が、前記中
間壁による濾過処理を受けた後、左槽に入り、そこから
送水ポンプ4バルブVを介して育成水槽2へ供給され
る。そして、ブロワー、もしくはコンプレッサー3か
ら、バルブV、育成用気体供給管65を介して導入さ
れた空気が旋回式エアレータ6を通過する間に微細気泡
となって育成用水1中に放出される。それに伴って装置
内に循環流が継続的に形成されるので、微細気泡による
接触表面積の増大化と微細気泡による液中浮遊時間の長
期化とにより、育成用水中の溶存酸素量は非常に増大
し、水生生物の育成環境が向上する。
Since the discharge from aquatic organisms floats up in the growing tank 2, the drainage containing the discharged water is taken out from the growing tank drainage outlet 21 through the drainage outlet pipe 22 to the growing tank drainage purification device 5. And introduce. Growth tank drainage purification device 5
Is divided into two tanks on the left and right by the filter cloth 51 and the filter sand 52 on the middle wall, and the wastewater introduced into the right tank enters the left tank after being filtered by the middle wall. It is supplied to the growing water tank 2 via the water feed pump 4 valve V 1 . Then, while the air introduced from the blower or the compressor 3 through the valve V 2 and the growth gas supply pipe 65 passes through the swirl aerator 6, it becomes fine bubbles and is discharged into the growth water 1. Along with this, a circulating flow is continuously formed in the device, so the amount of dissolved oxygen in the growing water greatly increases due to the increase in the contact surface area due to the fine bubbles and the prolonged floating time in the liquid due to the fine bubbles. However, the environment for growing aquatic organisms is improved.

【0012】上記水生生物育成装置においては、エアレ
ータとして図2以下に図示する内部に螺旋板を固着した
円筒体を使用しているため、まず散気管を用いる従来法
のような多大な圧力損失エネルギーを要しなく、そし
て、せん断力を利用して気液を細分化する方式のため
に、散気管の場合のような大直径の気泡が生じるのでは
なく、極めて微小直径の気泡と比較的大直径の気泡の二
種類が発生する。したがって、気泡と育成用水との接触
表面積が増大し、気体の水中への溶解効率が非常に向上
し、その結果、魚介類、海草類等の水生生物の育成を高
効率で実施し得るものとなる。図2は、本発明実施例の
水生生物育成装置に係る旋回式エアレータの円筒体部の
一部切欠斜視図である。図2において、60は円筒体、
61・・は螺旋板、62は螺旋板支持支柱、63は下方
開口部を縮小した気液導入部である。
In the above-mentioned aquatic organism growing apparatus, since a cylindrical body having a spiral plate fixed inside is used as an aerator as shown in FIG. 2 and thereafter, first of all, a large pressure loss energy as in the conventional method using a diffuser pipe is used. Because of the method of subdividing gas-liquid using shearing force without using air bubbles, bubbles with extremely small diameters and relatively large bubbles are generated instead of the bubbles with large diameters that occur in the case of diffuser tubes. Two types of bubbles of diameter are generated. Therefore, the contact surface area between the bubbles and the growing water is increased, and the dissolution efficiency of the gas in water is greatly improved, and as a result, it is possible to grow aquatic organisms such as seafood and seaweed with high efficiency. .. FIG. 2 is a partially cutaway perspective view of the cylindrical body portion of the swivel aerator according to the aquatic organism growing apparatus of the embodiment of the present invention. In FIG. 2, 60 is a cylindrical body,
61 ... Is a spiral plate, 62 is a spiral plate supporting column, and 63 is a gas-liquid introducing part with a lower opening reduced.

【0013】図3は、本発明実施例の水生生物育成装置
に係る旋回型エアレータの一部切欠取付斜視図であり、
図4(a)、(b)は平面図及び縦断面図であるる。こ
こで、気体(通常は空気)が気体供給管65より供給さ
れ、空気供給口66より、サポート64に取付られた旋
回式エアレータの円筒体60に供給される。なお、サポ
ート64と気体導入部63及び気体供給管65とは、強
力接着剤等による接着あるいは溶着により固着されてお
り、さらにそれらは、取付Uバンド68により、エアレ
ータ取付架台67に固定されて取付られている。同図に
おいて、育成用気体が気体供給管65内を矢印方向から
流れてくると、空気供給口66において空気塊となって
育成用水中に放出される。この空気塊はその浮力により
上昇する過程で63の気液導入部に導入され、螺旋板6
1・・に側って上昇しながら旋回を増す過程で、円筒体
内の旋回育成用水との間に形成されるせん断力で微細化
される。本例では、螺旋板61・・は、90゜間隔で4
枚取着されており、リード角βは1.0である。リード
角βは通常、0.7〜1.3程度が好ましい。次いで、
発生した微細気泡を含む気液二相流は、漸縮円筒体6
0’内で更にその上昇速度を増し、生物育成槽内に強力
で安定した循環流を連続して形成し、その全水域へ微細
気泡を運搬することとなる。
FIG. 3 is a partially cutaway perspective view of a swirl type aerator according to the aquatic organism growing apparatus of the embodiment of the present invention.
4A and 4B are a plan view and a vertical sectional view. Here, gas (usually air) is supplied from the gas supply pipe 65 and supplied from the air supply port 66 to the cylindrical body 60 of the swivel aerator attached to the support 64. The support 64, the gas introduction portion 63, and the gas supply pipe 65 are fixed to each other by adhesion or welding with a strong adhesive or the like, and they are fixed to the aerator mounting base 67 by a mounting U band 68. Has been. In the figure, when the growing gas flows in the gas supply pipe 65 in the direction of the arrow, it becomes an air mass at the air supply port 66 and is discharged into the growing water. This air mass is introduced into the gas-liquid introducing section 63 in the process of rising due to its buoyancy, and the spiral plate 6
In the process of increasing the swirl while rising toward 1 ..., the particles are atomized by the shearing force formed between the swirling water for growth in the cylindrical body. In this example, the spiral plates 61 ...
The sheets are attached, and the lead angle β is 1.0. Usually, the lead angle β is preferably about 0.7 to 1.3. Then
The gas-liquid two-phase flow containing the generated fine bubbles is reduced by the contracting cylindrical body 6
In 0 ′, the rising speed is further increased, a strong and stable circulating flow is continuously formed in the biological growth tank, and the fine bubbles are transported to the whole water area.

【0014】図5は、従来の単管曝気式エアレータによ
る発生気泡と実施例のエアレータによる発生気泡の気泡
径・気泡発生率等の分布図である。この場合の測定条件
は両者共、下記のとおりである。
FIG. 5 is a distribution chart of bubble diameters, bubble generation rates, etc. of bubbles generated by the conventional single tube aeration type aerator and bubbles generated by the aerator of the embodiment. The measurement conditions in this case are as follows.

【0015】本発明に係るエアレータの生物育成水内に
おける設置は、育成水域内に多数個を配設することも好
ましく、例えば3〜5個を一まとめにしたものを適宜距
離間隔を隔てて、育成水域の底部中央付近と右側付近と
に配設することにより、育成水域内に安定した強力な循
環流を生成せしめるようにすることもできる。
When the aerator according to the present invention is installed in the biological growth water, it is preferable that a large number of aerators are arranged in the growth water area. For example, a set of 3 to 5 pieces is arranged at appropriate intervals. It is also possible to generate a stable and strong circulating flow in the growing water area by arranging it near the center of the bottom of the growing water area and near the right side.

【0014】[0014]

【発明の効果】以上実施例等で詳述したように、本発明
によれば下記のごとき優れた多くの作用効果が発揮され
る。 (1)本発明に係るエアレータによれば、従来の噴き出
し方式のエアレータよりもかなり小さい圧力損失とな
り、育成用水中での気泡発生効率が飛躍的に向上する。 (2)従来の噴き出し方式ではセラミックス製等の不規
則多孔質管の細孔の径をミクロン程度に小さくしてもそ
こから発生する気泡の径は平均的に数ミリメートルほど
あったが、本発明に係る旋回式のエアレータによれば発
生する微細気泡の平均径を数100μmから数10μm
に微細化することができる。よって、育成用水と酸化ガ
ス等の気泡との接触面積を極端に増大することができ、
かつ気泡の育成用水中における滞留時間を著しく増長す
ることができ、その結果育成用水中への溶解酸素量を飛
躍的に増量することができる。 (3)漸縮円筒体の採用により、上昇気液二相流速が増
強され、水槽内に強力かつ安定した循環流を形成するこ
とができ、それが水生生物の育成に好ましい環境とな
る。この時、漸縮円筒体内には圧力損失がほとんどな
い。 (4)特に円筒体下部開口部が縮小したものにあって
は、気体の上昇に伴うエアリフト効果をさらに向上させ
るために、育成水域底付近に沈澱する残査等を巻き上
げ、水底付近の腐敗を防止することができる。 (5)高速回転羽根や突起体への衝突によってエアレー
ションを行う従来の方式では、水生生物などが破壊され
る問題があったが、本発明によればそうした問題はほと
んど発生しない。 (6)本発明に係る旋回式エアレータの空気供給口から
噴き出された空気塊は上昇連行過程で微細化されるので
該エアレータに目づまりはほとんど発生しない。
As described above in detail in the embodiments and the like, according to the present invention, many excellent effects as described below are exhibited. (1) According to the aerator of the present invention, the pressure loss is considerably smaller than that of the conventional jet type aerator, and the bubble generation efficiency in the growing water is dramatically improved. (2) In the conventional ejection method, even if the diameter of the pores of the irregular porous tube made of ceramics or the like is reduced to about micron, the diameter of the bubbles generated therefrom is about several millimeters on average. According to the swirl type aerator of the present invention, the average diameter of the fine bubbles generated is from several 100 μm to several 10 μm.
Can be miniaturized. Therefore, the contact area between the growing water and the bubbles such as the oxidizing gas can be extremely increased,
Moreover, the residence time of the bubbles in the growing water can be significantly increased, and as a result, the amount of dissolved oxygen in the growing water can be dramatically increased. (3) By adopting the taper cylinder, the ascending gas-liquid two-phase flow velocity is enhanced, and a strong and stable circulating flow can be formed in the water tank, which is a preferable environment for growing aquatic organisms. At this time, there is almost no pressure loss in the tapered cylinder. (4) In particular, in the case where the opening at the lower part of the cylindrical body is contracted, in order to further improve the air lift effect due to the rise of gas, the residue that precipitates near the bottom of the growing water area is rolled up to prevent spoilage near the bottom of the water. can do. (5) In the conventional method in which aeration is performed by the collision with the high-speed rotating blade or the protrusion, there is a problem that aquatic organisms are destroyed, but according to the present invention, such a problem hardly occurs. (6) Since the air mass ejected from the air supply port of the swirl type aerator according to the present invention is atomized in the ascending and entraining process, there is almost no clogging in the aerator.

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

【図1】本発明実施例に係る旋回式エアレータを備えた
水生生物育成装置の構成説明図
FIG. 1 is an explanatory diagram of a configuration of an aquatic organism growing apparatus including a swirl type aerator according to an embodiment of the present invention.

【図2】実施例旋回式エアレータの円筒体の一部切欠斜
視図
FIG. 2 is a partially cutaway perspective view of a cylindrical body of a swivel aerator according to an embodiment.

【図3】実施例旋回式エアレータの一部切欠取付斜視図FIG. 3 is a partially cutaway perspective view of the swivel aerator of the embodiment.

【図4】(a)及び(b)は、実施例旋回式エアレータ
の平面図及び縦断面図
4A and 4B are a plan view and a vertical cross-sectional view of a swivel aerator of an embodiment.

【図5】従来の単管曝気式エアレータと本発明実施例に
係る旋回式エアレータによる発生気泡の気泡径・気泡の
分布図
FIG. 5 is a bubble diameter / bubble distribution chart of bubbles generated by a conventional single-tube aeration type aerator and a swirl type aerator according to an embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1:水生生物育成水 2:水槽 21:育成槽排水取出口 22:排水導出管 3:ブロワー又はコンプレッサー 4:ポンプ 5:育成槽排水浄化装置 51:濾過布 52:濾過砂 53:浄化水移送管 6:旋回式エアレータ 60:円筒体 60’:漸縮円筒体 61:螺旋板 62:螺旋板支持支柱 63:気液導入部 64:サポート 65:気体供給管 66:空気供給口 67:エアレータ取付台 68:取付用Uバンド V、V:バルブ1: Aquatic organism breeding water 2: Water tank 21: Breeding tank drainage outlet 22: Drainage outlet pipe 3: Blower or compressor 4: Pump 5: Breeding tank drainage purification device 51: Filter cloth 52: Filtered sand 53: Purified water transfer pipe 6: Revolving aerator 60: Cylindrical body 60 ': Reduced cylindrical body 61: Spiral plate 62: Spiral plate support column 63: Gas-liquid introduction part 64: Support 65: Gas supply pipe 66: Air supply port 67: Aerator mount 68: U-band for mounting V 1 , V 2 : Valve

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 内壁に螺旋板を固着してなる円筒体と該
円筒体下方開口部直下に若干の間隔をおいて配置された
空気供給口とから構成される旋回式エアレータを水生生
物育成槽内に垂設してなることを特徴とする水生生物育
成装置。
1. A swirling aerator comprising a cylindrical body having a spiral plate fixed to an inner wall thereof and an air supply port arranged at a slight distance immediately below the lower opening of the cylindrical body. An apparatus for growing aquatic organisms, characterized by being laid vertically inside.
【請求項2】 円筒体が、その全体又は上方部が漸縮円
筒体であることを特徴とする請求項1記載の水生生物育
成装置。
2. The apparatus for growing aquatic organisms according to claim 1, wherein the whole or upper part of the cylindrical body is a gradually contracting cylindrical body.
【請求項3】 螺旋板が、多条のものであることを特徴
とする請求項1又は2に記載の水生生物育成装置。
3. The aquatic organism growing apparatus according to claim 1, wherein the spiral plate has a multi-row structure.
【請求項4】 円筒体内の中心軸に旋回板支持支柱を設
けたことを特徴とする請求項1ないし3のいずれかに記
載の水生生物育成装置。
4. The apparatus for growing aquatic organisms according to claim 1, wherein a swivel plate support column is provided on the central axis of the cylindrical body.
【請求項5】 円筒体下方開口部を縮小してなることを
特徴とする請求項1ないし4のいずれかに記載の水生生
物育成装置。
5. The aquatic organism growing apparatus according to claim 1, wherein the lower opening of the cylindrical body is reduced.
【請求項6】 円筒体内壁に固着される螺旋板が、複数
枚であり、リード角が0.7〜1.3であることを特徴
とする請求項1ないし5のいずれかに記載の水生生物育
成装置。
6. The aquatic plant according to claim 1, wherein the spiral plate fixed to the inner wall of the cylindrical body is a plurality of spiral plates and has a lead angle of 0.7 to 1.3. Biological equipment.
JP03335915A 1991-11-27 1991-11-27 Aquatic breeding equipment Expired - Fee Related JP3127536B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP03335915A JP3127536B2 (en) 1991-11-27 1991-11-27 Aquatic breeding equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP03335915A JP3127536B2 (en) 1991-11-27 1991-11-27 Aquatic breeding equipment

Publications (2)

Publication Number Publication Date
JPH05146236A true JPH05146236A (en) 1993-06-15
JP3127536B2 JP3127536B2 (en) 2001-01-29

Family

ID=18293790

Family Applications (1)

Application Number Title Priority Date Filing Date
JP03335915A Expired - Fee Related JP3127536B2 (en) 1991-11-27 1991-11-27 Aquatic breeding equipment

Country Status (1)

Country Link
JP (1) JP3127536B2 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0826640A3 (en) * 1996-08-10 1998-04-22 Robert Howard Smith A water oxygenating device
KR100465756B1 (en) * 2002-08-06 2005-01-13 조통래 air bubble solution apparatus
KR100915782B1 (en) * 2007-08-22 2009-09-04 박종후 Compacked Nanobubble Generating Apparatus
US7785476B2 (en) * 2008-02-13 2010-08-31 Tetra Holding (Us), Inc. Protein skimmer with stationary fan

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0826640A3 (en) * 1996-08-10 1998-04-22 Robert Howard Smith A water oxygenating device
KR100465756B1 (en) * 2002-08-06 2005-01-13 조통래 air bubble solution apparatus
KR100915782B1 (en) * 2007-08-22 2009-09-04 박종후 Compacked Nanobubble Generating Apparatus
US7785476B2 (en) * 2008-02-13 2010-08-31 Tetra Holding (Us), Inc. Protein skimmer with stationary fan

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Publication number Publication date
JP3127536B2 (en) 2001-01-29

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