JPH08132094A - Fine bubble discharger - Google Patents

Fine bubble discharger

Info

Publication number
JPH08132094A
JPH08132094A JP29892394A JP29892394A JPH08132094A JP H08132094 A JPH08132094 A JP H08132094A JP 29892394 A JP29892394 A JP 29892394A JP 29892394 A JP29892394 A JP 29892394A JP H08132094 A JPH08132094 A JP H08132094A
Authority
JP
Japan
Prior art keywords
discharge
cylinder
outer cylinder
liq
gas
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
JP29892394A
Other languages
Japanese (ja)
Other versions
JP2939704B2 (en
Inventor
Ryuichiro Naruse
龍一郎 成瀬
Kazuyoshi Hosoya
多慶 細谷
Yoshihiro Okabe
喜洋 岡部
Toshimitsu Nagayasu
利光 永安
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.)
AISAWA KOGYO KK
Morishita Chemical Industry Co Ltd
Original Assignee
AISAWA KOGYO KK
Morishita Chemical Industry 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 AISAWA KOGYO KK, Morishita Chemical Industry Co Ltd filed Critical AISAWA KOGYO KK
Priority to JP29892394A priority Critical patent/JP2939704B2/en
Publication of JPH08132094A publication Critical patent/JPH08132094A/en
Application granted granted Critical
Publication of JP2939704B2 publication Critical patent/JP2939704B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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

PURPOSE: To increase the discharge of a liq. contg. dissolved gas at the time of purifying the water in the closed waters, etc., to increase the content of fine bubbles in the discharge and to continuously discharge the fine bubbles. CONSTITUTION: A pressurized liq. contg. dissolved gas is supplied from one end of an inner cylinder 7, the other end is closed, and the cylinder is pierced with minute-inner-diameter injection holes 10. An outer cylinder 14 having a discharge port 16 and with which the liq. injected from the holes 10 is collided is provided outside the injection holes 10. The flow velocity of the liq. is suppressed by the injection from the holes 10 and the outer cylinder 14, the pressure is released at a breath, and many fine bubbles are discharged. When the original liq. is supplied to the device 1 through a pump, ejector and pressurized tank, the water is purified by the aeration, coagulated floc of fine bubbles and the adsorption and flotation of the suspended matter.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】この発明は、池、湖沼、湾などの
閉鎖性水域、或いは汚水処理プラントに於ける曝気や、
凝集フロック、浮遊物の吸着浮上による水質浄化に使用
するための微細気泡を排出する装置に関する。
This invention relates to aeration in a closed water area such as a pond, a lake, a bay, or a sewage treatment plant,
The present invention relates to a device for discharging fine bubbles for use in water purification by flocculating flocs and adsorbing and floating suspended matter.

【0002】[0002]

【従来の技術】下水道整備の遅れから、生活排水がその
まま垂れ流し状態で、河川や、河川を介して閉鎖性水域
へ流入している。とくに閉鎖性水域では水域が富栄養化
して、アオコと呼ばれる植物プランクトンの増殖、魚種
の変化、自然浄化能力の低下などの水質の悪化が取り沙
汰されるようになっている。
2. Description of the Related Art Due to the delay in the construction of sewers, domestic wastewater flows into the closed water area through rivers or rivers as it is. Especially in the closed water area, the water area becomes eutrophication, and the deterioration of the water quality such as the multiplication of phytoplankton called blue-green algae, the change of fish species, the deterioration of the natural purification capacity, etc. is becoming popular.

【0003】そこで、このような水質が悪化した閉鎖性
水域を、直接曝気を行うことによって、空気酸化による
有機物の分解能力を向上させ、水質の浄化を図ってい
る。又汚水処理プラントに於いても、汚水中の活性汚泥
に必要な空気(酸素)を十分に供給して汚水と活性汚泥
とを攪拌し、均一に懸濁させることにより汚泥の活性化
を促すために曝気を行っている。
Therefore, by directly aerating such a closed water area where the water quality is deteriorated, the ability of decomposing organic substances by air oxidation is improved to purify the water quality. Also in a wastewater treatment plant, in order to promote the activation of the sludge by sufficiently supplying the air (oxygen) necessary for the activated sludge in the wastewater, stirring the wastewater and the activated sludge, and uniformly suspending them. Is being aerated.

【0004】直接曝気、活性汚泥への曝気のいずれに於
いても、水中への酸素溶解を効率的に進行させることが
重要である。そのためには、水と空気との接触面積を可
能な限り大きくすることが必要であり、従って気泡の大
きさを微細にするほどその効果は大きくなる。
In both direct aeration and aeration to activated sludge, it is important to efficiently promote oxygen dissolution in water. For that purpose, it is necessary to make the contact area between water and air as large as possible. Therefore, the effect becomes larger as the size of the bubbles becomes smaller.

【0005】さらに、汚水処理プラントの汚濁水処理方
法の一つとして、汚濁水に凝集剤を添加して凝集フロッ
クを作り、その凝集フロックに微細な気泡を吸着させる
ことにより、凝集フロックを水面まで浮上させ、これを
回収して水質の浄化を図る方法がある。
Further, as one of the methods for treating polluted water in a sewage treatment plant, a flocculant is added to the polluted water to form flocculated flocs, and fine flocculated air bubbles are adsorbed to the flocculated flocs so that the flocculated flocs can reach the water surface. There is a method to raise water and collect it to purify the water quality.

【0006】又凝集フロックを利用する方法は、汚染さ
れた閉鎖性水域で直接実施する場合と、汚濁水をいった
ん汲み上げて処理プラントで処理したうえ、処理水を水
域内へ戻す場合とがある。さらに工場排水などは処理プ
ラントで処理される。いずれの場合でも、気泡が均一で
粒径が小さければ小さいほど、吸着率が高くかつ静かに
浮上し、しかも上層でバブリングしないため、吸着され
たフロックや浮遊物が壊れることなく回収できるもので
ある。
[0006] The method of utilizing the floc flocs may be carried out directly in a contaminated closed water area or in a case where polluted water is once pumped up and treated in a treatment plant and then the treated water is returned into the water area. Furthermore, industrial wastewater is treated at the treatment plant. In any case, the more uniform the bubbles and the smaller the particle size, the higher the adsorption rate and the quieter floating, and since bubbling does not occur in the upper layer, the adsorbed flocs and suspended matter can be recovered without being broken. .

【0007】ところで、水質浄化には曝気が必要である
が、空気などの気体溶解液を排水ホ−ス先端部から直
接、連続的に排出する方法では、一般的に前記先端部を
絞らない場合は、排出量は大きいが、圧力開放が一気に
行われず、ホ−ス内で徐々に行われるため、気泡の径が
大きくなり、排出時の微細気泡の排出量に占める割合が
少ない。
By the way, aeration is necessary for water purification, but in the method in which a gas-dissolved liquid such as air is directly and continuously discharged from the tip of the drain hose, the tip is generally not squeezed. Although the discharge amount is large, the pressure is not released all at once and is gradually performed in the hose, so that the diameter of the bubble becomes large and the ratio of the minute bubble to the discharge amount is small.

【0008】これに対し先端部を絞った場合には、絞り
方が中途半端であれば、排出時の流速が大きくなって、
排出後の圧力開放が一気に行われないため、気泡の径が
大きくなり、排出後の微細気泡の排出量に占める割合が
少なくなる。逆に極端に絞ると、流速が抑えられて微細
気泡の排出量に占める割合は大きくなるものの、排出量
が極端に少なくなる。
On the other hand, when the tip portion is squeezed, if the squeezing method is halfway, the flow velocity at the time of discharge increases,
Since the pressure release after discharge is not performed at once, the diameter of the bubble becomes large, and the ratio of the fine bubble after discharge to the discharged amount becomes small. On the other hand, if the flow rate is extremely narrowed, the flow rate is suppressed and the ratio of the minute bubbles to the discharge amount increases, but the discharge amount decreases extremely.

【0009】気体溶解液を排水ホ−スの先端部から直接
排出する方法にかわり、圧力制御弁を用いたバッチ式排
出装置による方法では、排出ホ−スの口径にかかわら
ず、微細気泡の1回に排出される排出量に占める割合は
大きい。しかし、排出が間欠的に行われるので、連続的
に排出する方法に比べて全体の排出量が少なくなるた
め、処理効率が悪い。そこで、連続的に排出する方式と
同等の排出量を確保するためには、装置の大型化が必要
となる。
In place of the method of directly discharging the gas solution from the tip of the drainage hose, a method of using a batch type discharge device using a pressure control valve is used, regardless of the diameter of the discharge hose. It makes up a large proportion of the total amount of emissions. However, since the discharge is performed intermittently, the total discharge amount is smaller than that in the method of discharging continuously, and the treatment efficiency is poor. Therefore, in order to secure the same amount of discharge as the continuous discharge method, it is necessary to increase the size of the device.

【0010】[0010]

【発明が解決しようとする課題】この発明が解決しよう
とする課題は、気体溶解液の排出量が大きく、しかも微
細気泡の排出量に占める割合を大きくするとともに、連
続的に排出させることにある。
SUMMARY OF THE INVENTION The problem to be solved by the present invention is to discharge a large amount of a gas-dissolved liquid, and to increase the ratio of the discharge amount of fine bubbles to a continuous discharge. .

【0011】[0011]

【課題を解決するための手段】この発明の微細気泡排出
装置の特徴は、一端から加圧された気体溶解液が供給さ
れ、他端を閉塞した内筒に微細内径の噴出孔群を貫設す
るとともに、少なくとも噴出孔群の外側に、少なくとも
気体溶解液の供給側と反対側とのいずれか一方が開放さ
れて排出口が形成され、かつ噴出孔群から噴出した気体
溶解液が衝突する外筒が設けられていることにある。
The feature of the fine bubble discharging apparatus of the present invention is that a pressurized gas dissolving liquid is supplied from one end and a fine inner diameter ejection hole group is provided in an inner cylinder closed at the other end. In addition, at least one of the supply side and the opposite side of the gas-dissolved liquid is opened outside the ejection hole group to form a discharge port, and the gas-dissolved liquid ejected from the ejection hole group collides with the outside. A cylinder is provided.

【0012】[0012]

【実施例】図1及び図2は、この発明の微細気泡排出装
置1を示す。2は接続筒で、後端部には後述の排出ホ−
ス28を着脱するホ−ス接続部3が、先端部には雄ネジ
4が設けられている。5は外筒接続筒で、外周には雄ネ
ジ6が設けられている。
1 and 2 show a micro-bubble discharging device 1 of the present invention. Reference numeral 2 is a connecting cylinder, and a discharge hose described later is provided at the rear end.
A hose connecting portion 3 for attaching and detaching the shoe 28 is provided, and a male screw 4 is provided at the tip portion. Reference numeral 5 is an outer cylinder connecting cylinder, and a male screw 6 is provided on the outer circumference.

【0013】7は内筒であって、後端部に設けられた雌
ネジ8が接続筒2の雄ネジ4に螺着して、接続筒2に取
付けられている。9は蓋で、先端部に固着されて内筒7
の先端部を閉塞している。
Reference numeral 7 is an inner cylinder, and a female screw 8 provided at a rear end portion is screwed onto a male screw 4 of the connecting barrel 2 and attached to the connecting barrel 2. Reference numeral 9 is a lid, which is fixedly attached to the front end of the inner cylinder 7
Has blocked the tip.

【0014】10は内筒7に一定間隔に貫設された多数
の噴出孔で、内径2ないし4mm、実施例では3mmの
微細小径である。これら噴出孔10は、その内周面に雌
ネジ11が設けられている(図2参照)。12は雄ネジ
部材のビス(又はボルト)で、適宜選択された排出孔1
0の雌ネジ11に着脱自在に螺着されて、噴出孔10を
閉塞するようになっている。
Reference numeral 10 designates a large number of ejection holes penetrating the inner cylinder 7 at regular intervals and having a fine small diameter of 2 to 4 mm, and 3 mm in the embodiment. Female threads 11 are provided on the inner peripheral surface of these ejection holes 10 (see FIG. 2). Reference numeral 12 is a screw (or bolt) of a male screw member, which is an appropriately selected discharge hole 1
It is detachably screwed to the female screw 11 of 0 to close the ejection hole 10.

【0015】13は複数枚の補強板であって、排出ホ−
ス接続筒2の外周と外筒接続筒5の内周とに固着されて
いる。
Reference numeral 13 denotes a plurality of reinforcing plates, which are discharge hoses.
It is fixed to the outer circumference of the connecting sleeve 2 and the inner circumference of the outer connecting sleeve 5.

【0016】14は外筒で、後端部には雌ネジ15が設
けられて、この雌ネジ15を外筒接続筒5の雄ネジ6に
螺着することにより、外筒14は外筒接続筒5に着脱自
在に取付けられ、ビス12による噴出孔10の開閉、内
筒7のメインテナンスができるようになっている。この
外筒14は、内筒7を内包して前部は内筒7の先方へ延
出するとともに、先端部は開放されて排出口16を形成
する。
Reference numeral 14 is an outer cylinder, and a female screw 15 is provided at the rear end portion. By screwing this female screw 15 onto the male screw 6 of the outer cylinder connecting cylinder 5, the outer cylinder 14 is connected to the outer cylinder. It is detachably attached to the cylinder 5 so that the ejection hole 10 can be opened and closed by screws 12 and the inner cylinder 7 can be maintained. The outer cylinder 14 encloses the inner cylinder 7 so that the front portion extends beyond the inner cylinder 7 and the front end portion is opened to form a discharge port 16.

【0017】なお、17は複数枚、実施例では3枚のス
ペ−サで、基部を内筒7の前端部に固着され、内筒7と
外筒14との間を区画している。
Reference numeral 17 denotes a plurality of spacers, three spacers in the embodiment, the base portion of which is fixed to the front end portion of the inner cylinder 7 to partition the inner cylinder 7 and the outer cylinder 14.

【0018】ここで、内筒7の外径をφ1、外筒14の
内径をφ2、又外筒接続筒5の後端と内筒7の最後尾の
噴出孔10aとの距離をL1、最先端の噴出孔10bと
外筒14先端との距離をL2とする。実験によると、φ
2≦2φ1、L2≧φ2とするのが好ましい。
Here, the outer diameter of the inner cylinder 7 is φ1, the inner diameter of the outer cylinder 14 is φ2, and the distance between the rear end of the outer cylinder connecting cylinder 5 and the rearmost ejection hole 10a of the inner cylinder 7 is L1. The distance between the ejection hole 10b at the tip and the tip of the outer cylinder 14 is L2. According to the experiment, φ
It is preferable that 2 ≦ 2φ1 and L2 ≧ φ2.

【0019】又、外筒接続筒5の後端部は開放されて外
筒14と連通して、第2排出口16´を形成しているの
で、例えば第2排出口16´を上にして使用する場合に
は、気体溶解液をここから排出することができる。この
場合、実験によるとL1≧φ2が好ましい。
Further, since the rear end portion of the outer cylinder connecting cylinder 5 is opened and communicates with the outer cylinder 14 to form the second discharge port 16 ', for example, the second discharge port 16' is turned upward. If used, the gaseous solution can be drained from here. In this case, according to experiments, L1 ≧ φ2 is preferable.

【0020】図3はこの発明の微細気泡排出装置1を用
いた閉鎖性水域(池)の浄化装置をを示す。21は水中
に設置されたストレ−ナ、22は吸引ホ−ス、Pは吸引
ホ−ス22に接続されたポンプである。24は凝集剤を
収容したタンクで、バルブ23を介して吸引ホ−ス22
に接続されている。このポンプPは、実施例では揚程8
5m、吐出口の内径2インチの5段タ−ビンポンプが用
いられている。25はエゼクタで、ポンプPに接続され
ている。26はエゼクタ25へ接続された加圧タンク
で、余剰空気抜き弁27を備えている。
FIG. 3 shows a purifying device for a closed water area (pond) using the fine bubble discharging device 1 of the present invention. 21 is a strainer installed in water, 22 is a suction hose, and P is a pump connected to the suction hose 22. 24 is a tank containing a flocculant, and a suction hose 22 is provided through a valve 23.
It is connected to the. This pump P has a head of 8 in the embodiment.
A 5-stage turbine pump having a discharge port of 5 m and an inner diameter of 2 inches is used. An ejector 25 is connected to the pump P. A pressure tank 26 is connected to the ejector 25, and is provided with a surplus air vent valve 27.

【0021】28は加圧タンク26へ接続された排出ホ
−スで、バルブ29を介して、水中に横向きに設置され
た微細気泡排出装置1へ接続されている。
A discharge hose 28 is connected to the pressure tank 26, and is connected via a valve 29 to the fine bubble discharge device 1 installed laterally in water.

【0022】そこで、ストレ−ナ21、吸引ホ−ス22
を通って、凝集剤とともにポンプPへ吸い込まれた原液
Wは、空気を吸い込むエゼクタ25で気液混合液となっ
て加圧タンク26へ送り込まれる。加圧タンク26内で
加圧された気液混合液は、気体溶解液となって加圧タン
ク26から送り出され、排出ホ−ス28によって微細気
泡排出装置1へ供給される。
Therefore, the strainer 21 and the suction hose 22
The stock solution W sucked into the pump P together with the coagulant is sent to the pressure tank 26 as a gas-liquid mixed solution by the ejector 25 sucking air. The gas-liquid mixed liquid pressurized in the pressure tank 26 becomes a gas solution, is sent out from the pressure tank 26, and is supplied to the fine bubble discharging device 1 by the discharge hose 28.

【0023】内筒7へ供給された気体溶解液は、多数の
微細な噴出孔10からの噴出と、外筒14により噴出孔
10からの噴出直後の流速が抑えられることによって、
一気に圧力を開放しながら排出口16から排出される。
その結果、気体溶解液に熔解されていた気体、即ち空気
は多数の微細気泡となって浮上する。
The gas-dissolved liquid supplied to the inner cylinder 7 is ejected from a large number of minute ejection holes 10 and the flow velocity immediately after ejection from the ejection holes 10 is suppressed by the outer cylinder 14,
The pressure is released all at once, and the gas is discharged from the discharge port 16.
As a result, the gas dissolved in the gas solution, that is, the air, becomes a large number of fine bubbles and floats.

【0024】実施例の場合、この微細気泡排出装置1は
内径2インチ、最後尾の噴出孔10aから最先端の噴出
口10bまでの長さが約30cmの内筒7には、120
個の噴出孔10が設けられており、60個の噴出孔10
を開放し、残りの60個をビス12で閉塞し、加圧タン
ク26内の圧力を4Kg/cm2 に保持した結果が、最
も排出量に占める微細気泡の割合が多かった。もとより
原液Wの性状、気体溶解液の気体溶解度や供給圧力、微
細気泡排出装置の大きさ等によって、噴出孔10の内
径、数は任意に選択できる。
In the case of the embodiment, the fine bubble discharging device 1 has an inner diameter of 2 inches, and the inner cylinder 7 having a length of about 30 cm from the rearmost ejection hole 10a to the frontmost ejection port 10b has 120.
60 ejection holes 10 are provided, and 60 ejection holes 10 are provided.
Was opened, the remaining 60 pieces were closed with screws 12, and the pressure in the pressure tank 26 was maintained at 4 Kg / cm 2. The result was that the proportion of fine bubbles in the discharged amount was the largest. Of course, the inner diameter and the number of the ejection holes 10 can be arbitrarily selected depending on the properties of the stock solution W, the gas solubility and supply pressure of the gas solution, the size of the fine bubble discharging device, and the like.

【0025】この実施例に於ける閉鎖性水域の透視度は
20センチであったが、本浄化装置による曝気及び凝集
フロックの吸着浮上により、透視度が150センチに向
上して、底が見えるようになった。
Although the transparency of the closed water area in this example was 20 cm, the transparency was improved to 150 cm by the aeration and the adsorption and flotation of the flocs of the flocs by this purifying device so that the bottom can be seen. Became.

【0026】[0026]

【発明の効果】この発明の微細気泡排出装置により、極
微細な気泡を大量に、しかも連続して発生させることが
できるので、水中への酸素溶解効率が高い。又、この装
置を用いた浄化装置では、凝集フロックや浮遊物への吸
着率が高く、浮上効率、ひいてはそれらの回収効率が非
常に高くなる。
With the device for discharging fine bubbles of the present invention, a large amount of extremely fine bubbles can be generated continuously and the efficiency of dissolving oxygen in water is high. Further, in the purification device using this device, the adsorption rate to the flocs of flocs and the suspended matter is high, and the floating efficiency, and thus the recovery efficiency thereof, are very high.

【0027】微細気泡排出装置は構造が簡単なため、取
扱い、メインテナンスが極めて容易であり、しかも安全
で低コストである。
Since the fine bubble discharging device has a simple structure, it is extremely easy to handle and maintain, and it is safe and low cost.

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

【図1】微細気泡排出装置の一部欠截側面図である。FIG. 1 is a partially cutaway side view of a fine bubble discharging device.

【図2】図1のA−A線断面図である。FIG. 2 is a sectional view taken along the line AA of FIG.

【図3】浄化装置の概念図である。FIG. 3 is a conceptual diagram of a purification device.

【符号の説明】[Explanation of symbols]

1 微細気泡排出装置 7 内筒 10 噴出孔 12 ビス 14 外筒 16 排出口 22 吸引ホ−ス 24 凝集剤を収容したタンク 25 エゼクタ 26 加圧タンク 28 排出ホ−ス P ポンプ W 原液 1 Micro Bubble Discharge Device 7 Inner Cylinder 10 Jet Hole 12 Screw 14 Outer Cylinder 16 Discharge Port 22 Suction Hoses 24 Tanks Containing Coagulant 25 Ejectors 26 Pressurized Tanks 28 Discharge Hoses P Pump W Undiluted Solution

───────────────────────────────────────────────────── フロントページの続き (72)発明者 岡部 喜洋 岡山県岡山市四御神463番地の1 (72)発明者 永安 利光 千葉県千葉市美浜区稲毛海岸3番1号 フ ラワ−ビル稲毛702号 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Yoshihiro Okabe 1 at 463 Shimikami, Okayama City, Okayama Prefecture (72) Inventor Toshimitsu Nagayasu No. 3 Inage Coast, Mihama-ku, Chiba City, Chiba Prefecture 702 Inage Flyer Building

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 一端から加圧された気体溶解液が供給さ
れ、他端を閉塞した内筒に微細内径の噴出孔群を貫設す
るとともに、少なくとも噴出孔群の外側に、少なくとも
気体溶解液の供給側と反対側とのいずれか一方が開放さ
れて排出口が形成され、かつ噴出孔群から噴出した気体
溶解液が衝突する外筒が設けられている微細気泡排出装
置。
1. A pressurized gas solution is supplied from one end, and a group of ejection holes having a fine inner diameter is provided in an inner cylinder having the other end closed, and at least the gas solution is provided at least outside the group of ejection holes. One of the supply side and the opposite side is opened to form a discharge port, and a fine bubble discharge device provided with an outer cylinder against which the gas-dissolved liquid ejected from the ejection hole group collides.
【請求項2】 噴出孔は、螺着される雄ネジ部材により
開閉可能である請求項1の微細気泡排出装置。
2. The fine bubble discharging device according to claim 1, wherein the ejection hole can be opened and closed by a male screw member screwed on.
【請求項3】 内筒の内径は、気体溶解液を供給する排
出ホ−スの内径と同程度に、外筒の内径は、内筒の外径
の2倍以下に形成されており、外筒は、排出口側に最近
の噴出孔から外筒の内径以上の長さで排出口側へ延出し
ている請求項1又は2の微細気泡排出装置。
3. The inner cylinder has an inner diameter that is approximately the same as the inner diameter of the discharge hose that supplies the gas-dissolved liquid, and the outer cylinder has an inner diameter that is not more than twice the outer diameter of the inner cylinder. 3. The fine bubble discharging device according to claim 1, wherein the cylinder extends toward the discharge port from a recent ejection hole at a length equal to or larger than the inner diameter of the outer cylinder.
JP29892394A 1994-11-07 1994-11-07 Fine bubble discharge device Expired - Fee Related JP2939704B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP29892394A JP2939704B2 (en) 1994-11-07 1994-11-07 Fine bubble discharge device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP29892394A JP2939704B2 (en) 1994-11-07 1994-11-07 Fine bubble discharge device

Publications (2)

Publication Number Publication Date
JPH08132094A true JPH08132094A (en) 1996-05-28
JP2939704B2 JP2939704B2 (en) 1999-08-25

Family

ID=17865940

Family Applications (1)

Application Number Title Priority Date Filing Date
JP29892394A Expired - Fee Related JP2939704B2 (en) 1994-11-07 1994-11-07 Fine bubble discharge device

Country Status (1)

Country Link
JP (1) JP2939704B2 (en)

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US6315893B1 (en) 1997-12-25 2001-11-13 Yoshiyuki Sawada Gas/liquid mixer with degasifier
WO2002053505A1 (en) * 2000-12-27 2002-07-11 Shiga Prefecture Device and method for of water purification
KR20020094738A (en) * 2001-06-13 2002-12-18 엔.피.테크놀로지 주식회사 Air bubble generating apparatus
JP2004505752A (en) * 2000-08-04 2004-02-26 シアロックス インコーポレイテッド Wastewater oxygenator and method
JP2006305494A (en) * 2005-04-28 2006-11-09 Ebara Corp Oxygen dissolving system
JP2007330906A (en) * 2006-06-15 2007-12-27 Nakajima Kogyo:Kk Water purification apparatus and water purification method
EP1885481A2 (en) * 2005-05-25 2008-02-13 The Board Of Trustees Of The University Of Arkansas System and method for dissolving gases in fluids and for delivery of dissolved gases
ITSA20090010A1 (en) * 2009-05-29 2009-08-28 Ars Nova S A S Di Franca Pipolo E C AVERAGE BUBBLE DIFFUSER FOR VENTILATION AND AGITATION LIQUAMI TO BE PURE.
JP2009195811A (en) * 2008-02-20 2009-09-03 Panasonic Electric Works Co Ltd Water clarification apparatus
US8919743B2 (en) 2004-05-25 2014-12-30 Board Of Trustees Of The University Of Arkansas System and method for dissolving gases in fluids and for delivery of dissolved gases
US9248415B2 (en) 2004-05-25 2016-02-02 Board Of Trustees Of The University Of Arkansas Systems and methods for maximizing dissolved gas concentration of a single species of gas from a mixture of multiple gases
US9315402B2 (en) 2004-05-25 2016-04-19 Board Of Trustees Of The University Of Arkansas Systems and methods for wastewater treatment
US9340438B2 (en) 2004-05-25 2016-05-17 Board Of Trustees Of The University Of Arkansas Systems and methods for delivering dissolved gases into force-main and gravity sewers
CN108483759A (en) * 2018-04-11 2018-09-04 西安建筑科技大学 A kind of same quality of groundwater purifier removed of turbid dirt
US10077418B2 (en) 2015-04-15 2018-09-18 Board Of Trustees Of The University Of Arkansas Method for improved rate and control of beverage carbonation with automatic shut-off
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01228597A (en) * 1988-03-09 1989-09-12 Shin Meiwa Ind Co Ltd Aeration stirring apparatus

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6315893B1 (en) 1997-12-25 2001-11-13 Yoshiyuki Sawada Gas/liquid mixer with degasifier
JP2012166192A (en) * 2000-08-04 2012-09-06 Therox Inc Apparatus and method for oxygenating wastewater
JP2004505752A (en) * 2000-08-04 2004-02-26 シアロックス インコーポレイテッド Wastewater oxygenator and method
WO2002053505A1 (en) * 2000-12-27 2002-07-11 Shiga Prefecture Device and method for of water purification
KR20020094738A (en) * 2001-06-13 2002-12-18 엔.피.테크놀로지 주식회사 Air bubble generating apparatus
US9315402B2 (en) 2004-05-25 2016-04-19 Board Of Trustees Of The University Of Arkansas Systems and methods for wastewater treatment
US8919743B2 (en) 2004-05-25 2014-12-30 Board Of Trustees Of The University Of Arkansas System and method for dissolving gases in fluids and for delivery of dissolved gases
US9340438B2 (en) 2004-05-25 2016-05-17 Board Of Trustees Of The University Of Arkansas Systems and methods for delivering dissolved gases into force-main and gravity sewers
US9248415B2 (en) 2004-05-25 2016-02-02 Board Of Trustees Of The University Of Arkansas Systems and methods for maximizing dissolved gas concentration of a single species of gas from a mixture of multiple gases
JP4559289B2 (en) * 2005-04-28 2010-10-06 株式会社荏原製作所 Oxygen dissolving apparatus and oxygen dissolving method
JP2006305494A (en) * 2005-04-28 2006-11-09 Ebara Corp Oxygen dissolving system
EP1885481A4 (en) * 2005-05-25 2012-11-21 Univ Arkansas System and method for dissolving gases in fluids and for delivery of dissolved gases
EP1885481A2 (en) * 2005-05-25 2008-02-13 The Board Of Trustees Of The University Of Arkansas System and method for dissolving gases in fluids and for delivery of dissolved gases
EP1885481B1 (en) * 2005-05-25 2016-01-20 The Board Of Trustees Of The University Of Arkansas Method for dissolving a gas in a liquid
JP2007330906A (en) * 2006-06-15 2007-12-27 Nakajima Kogyo:Kk Water purification apparatus and water purification method
JP2009195811A (en) * 2008-02-20 2009-09-03 Panasonic Electric Works Co Ltd Water clarification apparatus
ITSA20090010A1 (en) * 2009-05-29 2009-08-28 Ars Nova S A S Di Franca Pipolo E C AVERAGE BUBBLE DIFFUSER FOR VENTILATION AND AGITATION LIQUAMI TO BE PURE.
US10077418B2 (en) 2015-04-15 2018-09-18 Board Of Trustees Of The University Of Arkansas Method for improved rate and control of beverage carbonation with automatic shut-off
CN108483759A (en) * 2018-04-11 2018-09-04 西安建筑科技大学 A kind of same quality of groundwater purifier removed of turbid dirt
CN108483759B (en) * 2018-04-11 2024-03-08 西安建筑科技大学 Underground water quality purifying device capable of removing turbid dirt simultaneously
CN114682147A (en) * 2022-03-24 2022-07-01 湖南云中科技有限公司 Novel nanometer bubble generator

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