JPS60225628A - Apparatus for generating bubbles liquid - Google Patents

Apparatus for generating bubbles liquid

Info

Publication number
JPS60225628A
JPS60225628A JP59082705A JP8270584A JPS60225628A JP S60225628 A JPS60225628 A JP S60225628A JP 59082705 A JP59082705 A JP 59082705A JP 8270584 A JP8270584 A JP 8270584A JP S60225628 A JPS60225628 A JP S60225628A
Authority
JP
Japan
Prior art keywords
liquid
bubbles
bubble
nozzle
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.)
Pending
Application number
JP59082705A
Other languages
Japanese (ja)
Inventor
Kazutomo Yakura
矢倉 和致
Tetsushige Yakura
矢倉 哲滋
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP59082705A priority Critical patent/JPS60225628A/en
Publication of JPS60225628A publication Critical patent/JPS60225628A/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

Landscapes

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

Abstract

PURPOSE:To prevent the increase in the particle size of air bubbles, by providing a perforated pipe, which has a large number of fanwise fine apertures and is closed at the leading end thereof, in communication with the jet orifice of a jet nozzle. CONSTITUTION:In an air mixed liquid generation part A, water flowed into a liquid chamber 20 is converted to bubbles mixed water by air injected from an air nozzle 10 and flowed out to an outer cylinder 60 while passed through a large number of fanwise fine apertures 52. Subsequently, bubbles water flowed out to the outer cylinder 60 is flowed into the first pressure regulation chamber 70 of a bubbles water storate part C without generating the mutual coalescence of air bubbles caused by the generation of turbulent streams because there is no barrier plate nor a corner parter in a flowline. In the pressure regulation chamber 70, bubbles water flowed into the bottom part 71 thereof from the outer cylinder 60 passes through the top part 72 thereof to be successively sent to a pressure regulation tank 80.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、気泡液の発生装置、特に工場排水、船舶機関
区に発生する汚水等を処理する排水処理装置、油水分離
装置等に使用される気泡水を発生させるための装置に関
するものである。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a bubble liquid generation device, particularly a bubble liquid generator used in a wastewater treatment device for treating industrial wastewater, sewage generated in a ship's engine room, etc., an oil-water separation device, etc. The present invention relates to a device for generating water.

従来の技術 発明し、連続的に気泡液を発生させることに成功したが
、気泡液中の気泡が再結合して気泡粒度が大径化する欠
点があった。
Although the prior art was invented and succeeded in continuously generating a bubble liquid, there was a drawback that the bubbles in the bubble liquid recombined and the bubble particle size became large.

発明が解決しようとする問題点 そこで本発明者は、気泡粒度の細かい気泡液を製造する
段階において、気泡液中の気泡が再結合して気泡粒度が
大径化することを防止することに成功した。
Problems to be Solved by the Invention Therefore, the present inventor succeeded in preventing the bubbles in the bubble liquid from recombining and increasing the bubble particle size at the stage of producing a bubble liquid with a fine bubble particle size. did.

問題を解決するための手段 このため、本発明は、気体混合液体を噴射する噴射ノズ
ルの噴射口に連通して多数の末広がシ細孔を有し、先端
を閉管した多孔管を設けると共に該多孔管の外周を取り
囲んで該多孔管の末広がり細孔から流出した気泡液を次
の第1圧ノJ調整室に乱流を発生させることなく円滑に
流出できるように形成した外筒を設け、更に前記外筒か
ら流出した気泡液を底部に流入させて頂部に設けた多数
の末広が多細孔から流出できるようにした第1圧力調整
室を設け、前記第1圧力調整室の頂部から流出した気泡
液を圧力調整タンクに貯蔵できるようにした。
Means for Solving the Problems Therefore, the present invention provides a porous tube with a closed tip, which has a large number of pores that widen toward each other, and communicates with the injection port of an injection nozzle that injects a gas-mixed liquid. An outer cylinder is provided that surrounds the outer periphery of the porous pipe and is formed so that the bubble liquid flowing out from the pores that widen toward the end of the porous pipe can flow smoothly into the next first pressure adjustment chamber without generating turbulence, Furthermore, a first pressure adjustment chamber is provided in which the bubble liquid flowing out of the outer cylinder is allowed to flow into the bottom and flow out from a large number of diverging multi-pores provided at the top, and the bubble liquid flows out from the top of the first pressure adjustment chamber. The bubble liquid can be stored in a pressure adjustment tank.

作用 上記噴射ノズルから発生した気体混合液体は上記多孔管
と上記第1圧力調整室頂部の各末広が多細孔を通過する
際、気泡粒度は細粒化されると共に細粒化された気泡は
直ちに拡散するようになっているので気泡粒同志が再結
合する恐れはなく、また、多孔管から第1圧力調整室に
至る外筒は乱流を発生することがないので、外筒内を流
れる気泡液は気泡粒同志が再結合する恐れは少なく、気
泡粒度の細かい気泡液が連続的かつ安定的に圧力調整タ
ンクに貯蔵されることになる。
Function: When the gas mixture liquid generated from the injection nozzle passes through the perforated tube and the multi-pores that widen toward each other at the top of the first pressure adjustment chamber, the bubble particle size is made finer, and the finer bubbles are Since it is designed to diffuse immediately, there is no risk of bubble particles recombining with each other, and since the outer cylinder from the porous pipe to the first pressure adjustment chamber does not generate turbulence, the air flows inside the outer cylinder. In the bubble liquid, there is little risk of bubble particles recombining with each other, and the bubble liquid with fine bubble particle size is continuously and stably stored in the pressure adjustment tank.

実施例 本発明装置は、気体混合液体発生部A1気泡液安定部B
及び、気泡液貯蔵部Cを伽えている。気体混合液体発生
部Aは、気体ノズ/L’lO1気体ノズ/v10の噴出
口【1の外周に形成された液体室20、液体室20に噴
射口81を臨ませだ液体ノズル801気体ノズ/1’l
Oの噴出口【lの中心線延長方向に、液体室20に連通
して形成された気体混合液体の噴射ノズ/l’40から
なっている。気体ノズ/L/10の噴出孔11のテーパ
角度をα、気体混合液体の噴射ノズ/l/40のテーバ
部41のチズル40の内周面との交点Pまでの水平距離
を部42の水平距離を14、液体ノズ1lz80の中心
線延長線と気体ノズ/L’lOの中心線との交点と気8
− の中心線とのなす角度をqとすると、次の関係式が成立
するように形成される。
Embodiment The device of the present invention includes a gas mixed liquid generating section A1 a bubble liquid stabilizing section B.
And a bubble liquid storage section C is maintained. The gas mixed liquid generating section A includes a liquid chamber 20 formed on the outer periphery of a gas nozzle/L'lO1 gas nozzle/v10, and a liquid nozzle 801 having an injection port 81 facing the liquid chamber 20. 1'l
The gas-mixed liquid injection nozzle 40 is formed in communication with the liquid chamber 20 in the extending direction of the center line of the nozzle O [1]. The taper angle of the jet hole 11 of the gas nozzle/L/10 is α, and the horizontal distance from the taper part 41 of the gas mixture liquid jet nozzle/L/40 to the intersection point P with the inner circumferential surface of the nozzle 40 is the horizontal distance of the part 42. The distance is 14, and the intersection of the center line extension of the liquid nozzle 1lz80 and the center line of the gas nozzle/L'lO is 8
If the angle between − and the center line is q, the following relational expression is established.

10≦α〈80°、1°≦β〈80°、α≧β、q≦9
0°、0≦l l<L、、l12〉O,l 8≧0.1
4≧0、l 5≧ 0、20>β6〉I C−1ぐ■ご
9六−ト・−)なお、液体室20から噴射ノズ/L’4
0へ移行する角部22は、液体が層流と々るように滑ら
かな面取シ部を形成する。
10≦α〈80°, 1°≦β〈80°, α≧β, q≦9
0°, 0≦l l<L,, l12>O, l 8≧0.1
4≧0, l 5≧0, 20>β6〉I C-1
The corner 22 that transitions to 0 forms a smooth chamfer so that the liquid flows laminarly.

上記関係式で1°≦α〈80°としたのは気体ノ混合し
て微粒状気泡が連続的に発生するからである。αの値が
loよセも小さい場合は空気噴流は噴射ノズ/l/40
の孔内壁に衝突せず、突き抜けることとなる。αの値が
80″より大きい場合はαの値に関係なく拡散せず、気
体ノズ/l/10の細孔部12の直径と略同じ直径の流
れになる恐れがある。
The reason why 1°≦α<80° is set in the above relational expression is that gases are mixed and fine bubbles are continuously generated. If the value of α is small, the air jet will be equal to the jet nozzle/l/40
It will penetrate through the hole without colliding with the inner wall of the hole. If the value of α is larger than 80″, there is a risk that the gas will not diffuse regardless of the value of α, and the flow will have a diameter that is approximately the same as the diameter of the pore portion 12 of the gas nozzle/l/10.

また、l°≦β≦80°としたのは、βの値が1°より
4− 小さくても、まだ、80°よシ大きくても微粒状気泡の
発生が非常に少くなるからである。α≧βとしたのは噴
射ノズ/l/40の孔内壁面に気体ノズμm0の噴出孔
11からの噴射空気が衝突する角度で気体混合液体を噴
射しながら気泡を発生させるのに効果があるからである
。更に、0≦Jl<L及びe4≧0としたのは、噴射ノ
ズ/L’40の末広テーバ孔41内で流体が右又は左図
シに旋回しつつ流動するので、このとき液体と気体とは
攪拌されて気体が液体中に混合されることになるからで
率がよく、とのためe4の平行部が設け、これにより噴
射ノズ#40の入口において効率のよい流体の層流が形
成される。次にq≦90°及び15≧0としたのは、液
体ノズ/l/80が噴射ノズル40の入口において効率
のよい流体の層流形成に役立ように設けられる。また、
e2〉0及びぎ8≧Oとしだのはq≦90°の目的と同
じく流体の層流形成に役立ち、液体が液体室20内に充
満して気体ノズ/L/10の先端の周囲から噴射ノズル
40へ平均した水流が得られるからである。気泡安定部
Bは、気体混合液体の噴射ノズ/L’40の噴射口41
に連通した多孔管50及び多孔管50の外周を取シ囲む
と共に次の第1圧力調整室70に臨ませた外筒60とか
らなっている。多孔管50は、先端51を閉管すると共
に管に多数の第2図に示すような末広がυ細孔52が設
けられている。細孔52は、その人口径dよシ大きいD
を出口径とするテ志の再結合や乱流発生を極力防止でき
るように配慮されている。外筒60は、多孔管50の細
孔52から流出した気泡液を乱流を発生させることなく
第1圧力調整宰70に円滑に流出できるように形成され
て、流路には角部や邪魔板部を取シ除いている。気泡液
貯蔵部0は、第1圧力調整室7oとこれを取シ囲んだ圧
力調整タンク80とからなっている。第1圧力調整室7
0は、外筒6o先端から流出した気泡液を底部71に流
入できるようにすると共に頂部72に第2図に示すと略
同様な末広が#)細孔720を多数設けている。圧力調
整タンク80は、第1圧力調整室7oの頂部72よシ僅
かに高い位置に気泡液出口81を設けている。
The reason for setting l°≦β≦80° is that even if the value of β is 4-4 degrees smaller than 1°, the generation of microscopic bubbles will be extremely small even if the value is larger than 80°. The reason why α≧β is set is that it is effective in generating bubbles while injecting the gas mixture liquid at an angle at which the air jetted from the jetting hole 11 of the gas nozzle μm0 collides with the inner wall surface of the jetting nozzle /l/40. It is from. Furthermore, the reason for setting 0≦Jl<L and e4≧0 is that the fluid flows while turning to the right or left in the diverging taper hole 41 of the injection nozzle/L'40, so at this time, the liquid and gas are Since the gas is stirred and mixed into the liquid, the efficiency is good, so the parallel part of e4 is provided, thereby forming an efficient laminar flow of the fluid at the inlet of the injection nozzle #40. Ru. Next, q≦90° and 15≧0 are set so that the liquid nozzle/l/80 is provided at the inlet of the injection nozzle 40 to help form an efficient laminar flow of the fluid. Also,
When e2〉0 and 8≧O, Shida is useful for forming a laminar flow of the fluid, same as the purpose of q≦90°, and the liquid fills the liquid chamber 20 and is injected from around the tip of the gas nozzle/L/10. This is because an average water flow to the nozzle 40 can be obtained. The bubble stabilizing part B is the injection port 41 of the gas-mixed liquid injection nozzle/L'40.
It consists of a porous pipe 50 that communicates with the porous pipe 50 and an outer cylinder 60 that surrounds the outer periphery of the porous pipe 50 and faces the next first pressure adjustment chamber 70. The porous tube 50 has a closed tip 51 and is provided with a large number of υ pores 52 that widen toward each other as shown in FIG. The pore 52 has a population diameter D larger than its population diameter d.
It is designed to prevent recombination and turbulence as much as possible, with the exit diameter being . The outer cylinder 60 is formed so that the bubble liquid flowing out from the pores 52 of the porous pipe 50 can smoothly flow out into the first pressure adjustment tube 70 without generating turbulence, and the flow path is free from corners and obstructions. The board has been removed. The bubble liquid storage section 0 consists of a first pressure adjustment chamber 7o and a pressure adjustment tank 80 surrounding the first pressure adjustment chamber 7o. First pressure adjustment chamber 7
0 allows the bubble liquid flowing out from the tip of the outer cylinder 6o to flow into the bottom part 71, and the top part 72 is provided with a large number of pores 720 which widen toward the end and are substantially similar to those shown in FIG. The pressure adjustment tank 80 has a bubble liquid outlet 81 located at a slightly higher position than the top 72 of the first pressure adjustment chamber 7o.

82は圧力調整弁取付ねじ孔、88は余剰空気溢方b・
孔 出方取付ねじ孔、84は圧力計取付用塵である。
82 is the pressure regulating valve mounting screw hole, 88 is the surplus air overflow b.
The mounting screw hole 84 is a hole for mounting a pressure gauge.

従って、気体ノズ/l/10に加圧空気、液体ノズル8
0に加圧水が供給されると、気体混合液体発生部Aにお
いて、液体室20に流入する水は、気体ノズ)vloか
らの噴射空気によって気泡混合水にされて、気泡水安定
部Bの多孔p#50内に送シ込ま′れ、多数の末広が多
細孔52を通過して外@60に流出するが、細孔52を
通過すれば気泡混合水は更に気泡粒度の細かい気泡水と
なるが、この際細孔は末広がり状断面となっているので
、気泡は拡散されて細粒化された気泡同志の再結合が防
止される。次いで外筒に流出した気泡水は流路に邪魔板
や角部がないので乱流を発生して気泡同志の7− 再結合を発生することなく気泡液貯蔵部Cの第1圧力調
整搦70に流入される。気泡液貯蔵部Cの第1圧力調整
室70では、外筒60から底部71に流入した気泡水は
頂部72を通過して順次圧力調整タンク80に迭られる
が、気泡水が頂部72の末広が多細孔720を通過すれ
ば、気泡水中の気泡粒度は更に細粒化されるが、この際
、細孔は末広が多断面となっているので気泡は拡散され
て細粒化された気泡同志の再結合の恐れはない。かくし
て細粒化された気泡粒度の気泡水が圧力調整タンク80
で貯蔵され、必要に応じ各用途に供給されることになる
Therefore, the gas nozzle/l/10 has pressurized air, the liquid nozzle 8
When pressurized water is supplied to the gas-mixed liquid generating section A, the water flowing into the liquid chamber 20 is made into bubble-mixed water by the air jetted from the gas nozzle (vlo), and the water flows through the porous holes p of the bubble-water stabilizing section B. It is fed into #50, passes through a large number of widening multi-pores 52, and flows out to the outside @60, but after passing through the pores 52, the bubbly mixed water becomes bubbly water with finer bubble particle size. However, in this case, since the pores have a cross section that widens toward the end, the bubbles are diffused and recombination of the finely divided bubbles is prevented. Next, the bubble water flowing into the outer cylinder generates turbulent flow because there are no baffles or corners in the flow path, and the first pressure adjustment ratio 70 of the bubble liquid storage section C is generated without recombining the bubbles. is flowing into the country. In the first pressure adjustment chamber 70 of the bubble liquid storage section C, the bubble water that has flowed into the bottom 71 from the outer cylinder 60 passes through the top 72 and is sequentially transferred to the pressure adjustment tank 80. When passing through the multi-pores 720, the bubble size in the bubble water becomes even finer, but at this time, since the pores widen toward each other and have multiple cross-sections, the bubbles are diffused and the fine-grained bubbles form one another. There is no fear of recombination. The bubble water with the fine bubble particle size is then transferred to the pressure adjustment tank 80.
It will be stored and supplied for various uses as needed.

発明の効果 以上のように、本発明装置によって、気泡水を気泡細粒
化の際の気泡同志の再結合を防止しつつ連続的に安定的
に発生させることが可能となった。
Effects of the Invention As described above, the apparatus of the present invention makes it possible to continuously and stably generate bubble water while preventing the bubbles from recombining with each other during bubble refinement.

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

第1図は本発明の実施例を示す縦断面図、第2図は多孔
管の末広が多細孔の拡大断面図である。 lO・・・気体ノズル 8− 11・・・同噴出口 20・・・液体室 80・・・液体ノズル 81・・・同噴射口 40・・・気体混合液体の噴射ノズル 471・・・同噴射口 50・・・多孔管 51・・・同閉管 52・・・同末広が多細孔 60・・・外筒 70・・・第1圧力調整室 71・・・同底部 72・・・同頂部 720・・・末広が多細孔 80・・・圧力調整タンク 代理人 弁理士 渡 辺 弥 − lO− 特開昭GO−225628(4)
FIG. 1 is a longitudinal sectional view showing an embodiment of the present invention, and FIG. 2 is an enlarged sectional view of the multi-pores of the porous tube. lO...Gas nozzle 8-11...Same jet port 20...Liquid chamber 80...Liquid nozzle 81...Same jet port 40...Gas mixed liquid injection nozzle 471...Same injection Mouth 50...Porous tube 51...Closed tube 52...Multi-pores widening at the end 60...Outer cylinder 70...First pressure adjustment chamber 71...Bottom part 72...Top part 720...Multi-pores widening towards the end 80...Pressure adjustment tank agent Patent attorney Ya Watanabe - lO- JP-A-Sho GO-225628 (4)

Claims (1)

【特許請求の範囲】[Claims] 気体ノズルの噴出口の外周に液体室を形成して該液体室
に1又は2以上の液体ノズルの噴射口を臨ませると共に
前記気体ノズルの噴出口の中心線延長方向に、前記液体
室に連通ずる気体混合液体の噴射ノズルを形成すること
、前記気体混合液体の噴射ノズルの噴射口に連通して多
数の末広が多細孔を有し、先端を閉管した多孔管を設け
ると共に該多孔管の外周を取シ囲んで該多孔管の末広が
り細孔から流出した気泡液を次の第1圧力調整室に乱流
を発生させることなく円滑に流出できるように形成した
外筒を設けること、前記外筒から流出した気泡液を底部
に流入して頂部に設けた多数の末広が多細孔から流出で
きるようにした第1圧力調整室を形成すると共に前記第
1圧力調整室の頂部から流出した気泡液を流入できるよ
うにした圧力調整タンクを設けることからなることを特
徴とした気泡液発生装置。
A liquid chamber is formed on the outer periphery of the ejection port of the gas nozzle, and the ejection ports of one or more liquid nozzles are made to face the liquid chamber, and the ejection port of the gas nozzle is connected to the liquid chamber in the direction in which the center line of the ejection port of the gas nozzle extends. forming a gas-mixed liquid injection nozzle that communicates with the gas-mixed liquid injection nozzle; a porous tube having a large number of diverging multi-pores and having a closed tip connected to the injection port of the gas-mixed liquid injection nozzle; providing an outer cylinder that surrounds the outer periphery and is formed so that the bubble liquid flowing out from the widening pores of the porous tube can smoothly flow into the next first pressure adjustment chamber without generating turbulence; A first pressure adjustment chamber is formed in which the bubble liquid flowing out of the cylinder flows into the bottom and flows out from a large number of widening pores provided at the top, and the air bubbles flow out from the top of the first pressure adjustment chamber. A bubble liquid generator characterized by comprising a pressure regulating tank into which liquid can flow.
JP59082705A 1984-04-24 1984-04-24 Apparatus for generating bubbles liquid Pending JPS60225628A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59082705A JPS60225628A (en) 1984-04-24 1984-04-24 Apparatus for generating bubbles liquid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59082705A JPS60225628A (en) 1984-04-24 1984-04-24 Apparatus for generating bubbles liquid

Publications (1)

Publication Number Publication Date
JPS60225628A true JPS60225628A (en) 1985-11-09

Family

ID=13781816

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59082705A Pending JPS60225628A (en) 1984-04-24 1984-04-24 Apparatus for generating bubbles liquid

Country Status (1)

Country Link
JP (1) JPS60225628A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0544289U (en) * 1991-11-22 1993-06-15 祥司 豊田 Ozone mixing equipment
JP2009082906A (en) * 2007-09-12 2009-04-23 Yamaha Motor Co Ltd Bubble generator and bubble generation device
CN102210987A (en) * 2010-04-12 2011-10-12 阿思普株式会社 Gas dissolving liquid generation device and generation method therefor
JP2014514132A (en) * 2011-03-04 2014-06-19 ポドマジェルスキー,カール Method and apparatus for generating water bubbles or bubbles

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0544289U (en) * 1991-11-22 1993-06-15 祥司 豊田 Ozone mixing equipment
JP2009082906A (en) * 2007-09-12 2009-04-23 Yamaha Motor Co Ltd Bubble generator and bubble generation device
CN102210987A (en) * 2010-04-12 2011-10-12 阿思普株式会社 Gas dissolving liquid generation device and generation method therefor
JP2011218308A (en) * 2010-04-12 2011-11-04 Asupu:Kk Gas-dissolved liquid generating apparatus and method for generation
JP2014514132A (en) * 2011-03-04 2014-06-19 ポドマジェルスキー,カール Method and apparatus for generating water bubbles or bubbles

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