JP2009160576A - Fine air bubble generator - Google Patents

Fine air bubble generator Download PDF

Info

Publication number
JP2009160576A
JP2009160576A JP2008336044A JP2008336044A JP2009160576A JP 2009160576 A JP2009160576 A JP 2009160576A JP 2008336044 A JP2008336044 A JP 2008336044A JP 2008336044 A JP2008336044 A JP 2008336044A JP 2009160576 A JP2009160576 A JP 2009160576A
Authority
JP
Japan
Prior art keywords
liquid
fine bubble
outlet
cylindrical
swirl chamber
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
JP2008336044A
Other languages
Japanese (ja)
Other versions
JP4636420B2 (en
Inventor
Yasumasa Nishiyama
康正 西山
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 JP2008336044A priority Critical patent/JP4636420B2/en
Publication of JP2009160576A publication Critical patent/JP2009160576A/en
Application granted granted Critical
Publication of JP4636420B2 publication Critical patent/JP4636420B2/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Abstract

<P>PROBLEM TO BE SOLVED: To solve problems, such as loud noises, a pump with larger power, a large scale as the total system, and high cost,in conventional fine air bubble generators, which cannot produce a large amount of fine air bubbles without imparting a high feed pressure. <P>SOLUTION: A fluid in a circling chamber is smoothly circled to make a high circling angular velocity by reducing friction resistance in the circling chamber and shaping the circling chamber not to generate an excess acceleration, and installing a vane shaped nozzle, a preliminary circling chamber and then a guide vane smoothly changing the flow direction of a fluid from an introducing opening on the outer periphery of the circling chamber. Then, air bubbles large in a diameter are selectively sheared again by installing a cylindrical-shaped cover for circulation just after the outlet opening of the circling chamber. Further, unfoamed liquid in which foams are dissolved in the liquid are made to pass through a flow passage accelerating depressurized foaming. Thereby, a large amount of fine air bubbles are generated even by low consumption energy. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

本発明は主に、水槽や浴槽、養殖池等の水中又は気液反応槽の液中に微細な気泡を多量に発生させる微細気泡発生装置に関する。  The present invention mainly relates to a fine bubble generating apparatus that generates a large amount of fine bubbles in water or a liquid in a gas-liquid reaction tank such as a water tank, a bathtub, or a culture pond.

近年、微細な気泡を水中に発生させる事により、水の浄化、浄化の補助、水中への溶存酸素増加手段、又は、気液反応槽の反応速度、反応効率を向上させたり、ペットや人の浴槽に微細な気泡を発生させマッサージ効果や温熱効果や洗浄効果を得たり、部品等の汚れを取り除く等の研究、開発、商品化が行われているが、多量に微細な気泡を発生させるには、高い供給圧力が必要であった。  In recent years, by generating fine bubbles in water, purification of water, assistance in purification, means for increasing dissolved oxygen in water, or the reaction speed and reaction efficiency of gas-liquid reaction tanks, Research, development, and commercialization have been carried out, such as generating fine bubbles in the bathtub to obtain a massage effect, thermal effect and cleaning effect, and removing dirt from parts, etc., but in order to generate a large amount of fine bubbles Required a high supply pressure.

従来の微細気泡発生装置の旋回室の形状として例えば、特開2000−000447号公報には、「円錐形、円錐台形、徳利形状又はワインボトル形状のスペースを有する容器本体と、同スペースの内壁円周面の一部にその接線方向に開設された加圧液体導入口と」が開示されている。  As the shape of the swirl chamber of the conventional fine bubble generating device, for example, Japanese Patent Laid-Open No. 2000-000447 discloses a container body having a conical, frustoconical, bottle-shaped or wine bottle-shaped space, and an inner wall circle of the same space. And a pressurized liquid inlet opened in a tangential direction to a part of the peripheral surface.

特許3682286号公報には「略回転対称に形成され回転対称軸の軸方向の一方又は双方に向かって縮径した中空部を有する器体と、前記器体の周壁部に接線方向に開口された気液導入孔と」が開示されている。  In Japanese Patent No. 3682286, “a container body having a hollow portion that is formed substantially rotationally symmetric and has a diameter reduced toward one or both of the axial directions of the rotational symmetry axis, and a tangential opening is formed in the peripheral wall portion of the container body. “Gas-liquid introduction hole” is disclosed.

特開2004−195393号公報には「内部に円形の液室を形成した短い筒体の一端を端壁で閉じ、他端は液室に連通する所定径の開口を設け、断面を略鈎形コ字状とした混合筒から成り、この混合筒には液室の外周の接線方向に液室と連通するように設けた外部から水を導入するための導水管と」が開示されている。  Japanese Patent Application Laid-Open No. 2004-195393 discloses that “one end of a short cylinder having a circular liquid chamber formed therein is closed with an end wall, and the other end is provided with an opening of a predetermined diameter communicating with the liquid chamber, and the cross section is substantially bowl-shaped. A mixing tube having a U-shape is disclosed, and a water guide pipe for introducing water from the outside provided to communicate with the liquid chamber in a tangential direction of the outer periphery of the liquid chamber is disclosed.

特開2006−142300号公報には「円筒状のケーシング内部に形成された気液の旋回可能な空間である気液旋回室と(途中省略)液体導入口は、この二重円筒構造部分の液体供給円筒の周壁面の上方に設けられ、前記二重円筒構造部分のケーシングと液体供給円筒との間に形成される空間が、前記液体導入口から導入された液体によって発生する旋回流を整流する予備旋回部を構成し」が開示されている。  Japanese Patent Laid-Open No. 2006-142300 discloses that “a gas-liquid swirl chamber, which is a gas-liquid swirl space formed inside a cylindrical casing, and a (liquid omitted) liquid introduction port are liquids of this double cylindrical structure portion. A space provided between the casing of the double cylindrical structure and the liquid supply cylinder provided above the peripheral wall surface of the supply cylinder rectifies the swirling flow generated by the liquid introduced from the liquid inlet. The preliminary swivel portion is configured ".

特開2006−015312号公報には「液体の流入のための第1の入口と、気体の流入のための第2の入口と、気体を混合させた液体を旋回せしめるハウジング(ハウジングの内周はインボリュート様曲線に沿った形状をなしている)と」が開示されている。  Japanese Patent Application Laid-Open No. 2006-015312 discloses a “first inlet for inflow of liquid, a second inlet for inflow of gas, and a housing for swirling liquid mixed with gas (the inner circumference of the housing is And a shape along an involute-like curve).

特開2007−237155号公報には「円筒型の胴に円形凹レンズ様の内室を有し、内壁円周部の接線方向に乱れなく沿って、旋回流が形成するよう内室円周部に、胴と平行に、細隙を開け、加圧した液体の導入口とし」が開示されている。  Japanese Patent Application Laid-Open No. 2007-237155 states that “the cylindrical body has a circular concave lens-like inner chamber, and the inner chamber circumferential portion forms a swirl flow along the tangential direction of the inner wall circumferential portion without being disturbed. In addition, a slit is opened in parallel with the cylinder to provide a pressurized liquid inlet ”.

特開2007−111616号公報には「旋回流が生じ得る空間(空間は、円柱または円錐状)を有する容器と、前記空間内に旋回流を生じさせる加圧液体を前記容器内へ導くように前記容器の側面に設けられた加圧液体導入口と」が開示されている。
特開2000−000447号公報 特許3682286号公報 特開2004−195393号公報 特開2006−142300号公報 特開2006−015312号公報 特開2007−237155号公報 特開2007−111616号公報
Japanese Patent Application Laid-Open No. 2007-111616 discloses that a container having a space in which a swirling flow can be generated (a space is a cylinder or a cone) and a pressurized liquid that generates the swirling flow in the space are guided into the container. And a pressurized liquid inlet provided on a side surface of the container.
JP 2000-000447 A Japanese Patent No. 3682286 JP 2004-195393 A JP 2006-142300 A JP 2006-015312 A JP 2007-237155 A JP 2007-111616 A

しかしながら、上記従来技術は以下の課題を有している。
図19に示すように、特許文献4を除く従来技術では、加圧流体が旋回流を起こす旋回室に突入する導入口の流速は2m/秒前後であることと、外周の低速域600では摩擦抵抗もあることや、特許文献4では、導入方向と旋回方向に角度があり運動エネルギーの無駄と乱流を起こす、また、殆んどのものが旋回室の径に対して、突入流の径の割合が大のため、旋回角速度が増速される増速域601の実質的な径が少なくなり、旋回流の導出口での旋回速度が低くなっている、これを解消するために、加圧流体の供給圧力を高くする必要があった。
However, the above prior art has the following problems.
As shown in FIG. 19, in the prior art except for Patent Document 4, the flow velocity of the inlet that enters the swirling chamber where the pressurized fluid causes a swirling flow is around 2 m / sec. There is also resistance, and in Patent Document 4, there is an angle between the introduction direction and the swirl direction, causing kinetic energy waste and turbulence, and most of them have a diameter of the rush flow relative to the swirl chamber diameter. Since the ratio is large, the substantial diameter of the acceleration region 601 where the turning angular velocity is increased is reduced, and the turning speed at the turning flow outlet is reduced. To eliminate this, pressurization is performed. It was necessary to increase the supply pressure of the fluid.

また、旋回室の形状も、円柱状、円錐形、円錐台形、徳利形状、ワインボトル形状、球状、砲弾状、半球状、短筒状、外周がインボリュート形状、凹レンズ状と様々あるが、導入口から旋回室に入り旋回運動をする液体は、壁面の不必要な摩擦抵抗以外にも、不必要な減速、加速による加速度が発生する形状となっており、より多くのエネルギーが必要となり、上記と同様に加圧流体の供給圧力を高くする必要があった。  In addition, the swirl chamber has various shapes such as a cylindrical shape, a conical shape, a truncated cone shape, a bottle shape, a wine bottle shape, a spherical shape, a bullet shape, a hemispherical shape, a short cylindrical shape, an involute shape on the outer periphery, and a concave lens shape. In addition to unnecessary frictional resistance on the wall, the liquid that enters the swirl chamber has a shape that generates unnecessary deceleration and acceleration due to acceleration, and requires more energy. Similarly, it is necessary to increase the supply pressure of the pressurized fluid.

さらに、多くのタイプで歪んだ旋回流で不必要な乱流発生と気泡のせん断による振動、騒音が大きいという問題があった。  Furthermore, many types of distorted swirling flow have the problem of unnecessary generation of turbulent flow and large vibration and noise due to bubble shearing.

また、一例として、牛乳風呂の様な浴槽用高濃度の発生装置として商品化されている機器の微細気泡発生器への供給圧力は、低圧のものでも0.26MPa程度とエネルギーを多く消費し、ポンプ等の周辺装置が高出力となり、大型、高価となっていた。  In addition, as an example, the supply pressure to the fine bubble generator of equipment that is commercialized as a high concentration generator for bathtubs such as a milk bath consumes a lot of energy as low as about 0.26 MPa, Peripheral devices such as pumps have high output, and are large and expensive.

なお、旋回式の微細気泡発生装置の特性として、液体の導出口での旋回速度を早めると、気泡のサイズが小さくなり、供給気体の量を増やすと、気泡のサイズが大きくなる、という特性がある。  In addition, as a characteristic of the swirling type fine bubble generating device, if the swirling speed at the liquid outlet is increased, the bubble size decreases, and if the amount of supply gas is increased, the bubble size increases. is there.

本発明は、上記課題に鑑みなされたものであり、その目的は、より少ない動力で、より多くの、より有効な50ミクロン前後の径の、微細気泡を発生させ、かつ、振動、騒音の発生を抑制した、微細気泡発生装置を開発し、微細気泡発生システム全体を、コンパクト化し、低価格で、提供することである。  The present invention has been made in view of the above-mentioned problems, and its object is to generate more effective, fine bubbles having a diameter of around 50 microns with less power, and to generate vibration and noise. To develop a microbubble generator that suppresses the above, and to make the entire microbubble generator system compact and provide it at low cost.

本発明の微細気泡発生装置は、単位体積当りの液中に微細気泡を増加させるために考案されたもので、これを達成するには、限られた動力で、旋回した液体の導出口での旋回速度をより高速とし、せん断力を高める必要がある。  The fine bubble generating apparatus of the present invention was devised to increase the fine bubbles in the liquid per unit volume. To achieve this, the liquid at the outlet of the swirling liquid with limited power is used. It is necessary to increase the turning speed and the shearing force.

その為には、液体導入口より供給された液体の運動エネルギー、圧力エネルギーを有効に使う様、液体が高速運動をしている旋回室での摩擦抵抗の削減、減速によるエネルギーロスの削減、旋回流に余分な加速度を発生させない旋回室の形状、流れ方向を滑らかにする事により、可能となる。本発明者は、次の方策を考案した。  To that end, to effectively use the kinetic energy and pressure energy of the liquid supplied from the liquid inlet, the frictional resistance is reduced in the swirling chamber where the liquid is moving at high speed, the energy loss is reduced due to deceleration, and the swirl This is possible by smoothing the shape and direction of the swirl chamber that does not generate excessive acceleration in the flow. The inventor has devised the following measures.

本発明の請求項1に記載の微細気泡発生装置は、図1、図2に示すように、旋回室外周部に取り付けられたノズル幅と同じ幅W1に周長を乗じた面積と、中間部の幅W2に周長を乗じた面積と、導出部の幅W3に周長を乗じた面積とが同じになる様な曲面をもたせ、ノズルから噴出した速度と1周目、2周目、n周目の流速をほぼ同じにすることで、旋回流に余分な加速度が生じない様、成型され、略、高さの違う富士山の輪郭を二重に重ねて出来る中間の空間様の前壁、後壁を持つ主旋回室を備える。  As shown in FIGS. 1 and 2, the fine bubble generator according to claim 1 of the present invention has an area obtained by multiplying the same width W1 as the nozzle width attached to the outer periphery of the swirl chamber by the peripheral length, and an intermediate portion. The surface obtained by multiplying the width W2 by the circumference and the area obtained by multiplying the width W3 of the lead-out portion by the circumference have the same curved surface, and the velocity ejected from the nozzle and the first and second rounds, n By making the flow velocity around the circumference almost the same, the front wall is like an intermediate space that is shaped and overlapped with the outline of Mt. A main swirl chamber with a rear wall is provided.

なお、従来技術では様々な旋回室の形状があるが、旋回流速度に加速度が付き、結果的に抵抗となり、供給圧力を高める必要がある。  Although there are various swirl chamber shapes in the prior art, it is necessary to increase the swirling flow velocity, resulting in resistance and increasing the supply pressure.

また前壁の頂部に当る位置の中心線上に高速旋回する液体の導出口を穿孔し、旋回室から開放端までの寸法を1mm前後と極力短くし、最高回転となる液体とケースとの間で発生する摩擦抵抗を少なくしている。  In addition, a liquid outlet for high-speed swirling is drilled on the center line at the position where it hits the top of the front wall, and the dimension from the swirling chamber to the open end is as short as about 1 mm. Reduced frictional resistance.

なお、従来技術ではこれが、数mmから約10mmと長く、放出するまで、旋回角速度が減速されていた。  In the prior art, this is as long as several mm to about 10 mm, and the turning angular velocity has been reduced until release.

また主旋回室の外周に、その接線方向に向け薄い帯板状の噴流を発生する一定速または、流入部より流出部の面積を序々に減少させ、噴流を増速させる機能を備えた10箇所前後のベーン状ノズルが取り付けられている。これにより、旋回室での旋回が乱れる事無く旋回角速度が増速され高速となる。また導出口における旋回角速度にあわせた、旋回室外周での初期流速を任意に決めることが出来る為、流量に合わせた設計が可能となる。  In addition, 10 locations on the outer periphery of the main swirl chamber that have a function of increasing the jet flow at a constant speed for generating a thin strip-shaped jet in the tangential direction or by gradually reducing the area of the outflow portion from the inflow portion. Front and rear vane nozzles are installed. As a result, the turning angular velocity is increased and the turning speed is increased without disturbing turning in the swirl chamber. In addition, since the initial flow velocity on the outer periphery of the swirl chamber can be arbitrarily determined in accordance with the swirling angular velocity at the outlet, the design according to the flow rate becomes possible.

なお、従来技術では、その殆んどが、処理水量に依り決まる導入口のサイズに合わせた内径のまま、旋回室に噴出されており、旋回室の外周部は、広い接触面で発生する摩擦抵抗もあり、流速が一旦、減速され、その後、小径の範囲で、旋回角速度の増速がおこなわれ、結果的に、旋回角速度が、高くなりにくい物であった。  In the prior art, most of the air is blown into the swirl chamber while maintaining the inner diameter that matches the inlet size determined by the amount of treated water, and the outer periphery of the swirl chamber has friction generated on a wide contact surface. There was also resistance, the flow velocity was once decelerated, and then the turning angular velocity was increased in the small diameter range. As a result, the turning angular velocity was difficult to increase.

また、その外周に液体導入口よりベーン状ノズルへ滑らかに且つ均等に液体が導かれる様成型された予旋回室を備えている。この液体導入口の内径は同一径もしくは、先細りとさせ流速を早くさせる構造としてもよい。  In addition, a pre-swirl chamber is formed on the outer periphery so that the liquid is smoothly and evenly guided from the liquid inlet to the vane nozzle. The inner diameter of the liquid introduction port may be the same diameter or may be tapered to increase the flow velocity.

また、従来技術では、ノズル周辺の外周との摩擦抵抗で旋回速度が低減されていたが、本発明では、旋回室外周部の厚さW1をベーン状ノズルの幅と同じ寸法にする事で、噴流の速度が有効に旋回運動のために使われる。  In the prior art, the swirl speed was reduced by the frictional resistance with the outer periphery around the nozzle, but in the present invention, the thickness W1 of the outer periphery of the swirl chamber is the same as the width of the vane nozzle, The velocity of the jet is effectively used for the swivel motion.

また、主旋回室の後壁の中心付近に凸部を設け、中心に向かった旋回流を、導出口へ、滑らかに、方向変換させる様にしている。  Further, a convex portion is provided in the vicinity of the center of the rear wall of the main swirl chamber so that the swirl flow toward the center is smoothly redirected to the outlet.

上記、構造とする事で、中心部の旋回角速度が十分に高速度となり、遠心力、向心力が働き、中心線上に、気柱軸が発生する。旋回流が導出口で最高回転となり外部に放出される。この時、粘性で気柱軸の気体を引き千切り、巻き込んで磨り潰し、気泡をせん断し、微細気泡を多量に発生させることができる様にした微細気泡発生装置である。  With the above structure, the turning angular velocity at the center becomes sufficiently high, centrifugal force and centripetal force work, and an air column axis is generated on the center line. The swirling flow reaches the maximum rotation at the outlet and is discharged to the outside. At this time, it is a fine bubble generator capable of generating a large amount of fine bubbles by drawing the gas of the air column shaft into a viscous, entangled and crushed, and shearing the bubbles.

本発明の請求項2に記載の微細気泡発生装置は、図3に示すように、請求項1に記載の微細気泡発生装置において、後壁部を取り去り、その面で対称になる様、背中合わせに設置し、ベーン状ノズルの方向を統一させ、液体導入口を1箇所とし、主旋回室の空間は、両吸込渦巻ポンプの羽根車の輪郭の形状をした、請求項1に記載の前壁部を2個とし、結果、導出口は2箇所となる、予旋回室を備えたベーン状ノズル部1組の少ない部品で2倍の流量の処理が可能となる、微細気泡発生装置である。As shown in FIG. 3, the microbubble generator according to claim 2 of the present invention is the microbubble generator according to claim 1, in which the rear wall is removed and the surfaces are symmetrical to each other so as to be symmetrical. The front wall portion according to claim 1, wherein the front wall portion is installed, the direction of the vane-shaped nozzle is unified, the liquid inlet is provided at one place, and the space of the main swirl chamber is in the shape of the outline of the impeller of both suction centrifugal pumps. The result is a fine bubble generator that can process twice the flow rate with a small number of parts with one set of vane-shaped nozzle portions equipped with a pre-swirl chamber.

本発明の請求項3に記載の微細気泡発生装置は、図4に示すように、高速旋回する液体の導出口の直後に、後壁の付いた、周上に複数の穴が穿孔された内径が導出口と同程度の筒状体を持つ蓋、または、その穴より外部側は円錐状に拡大された内径が導出口と同程度の筒状体を持つ蓋を設置し、導出口より放出された微細気泡を含む膜状となった気液が通過出来、かつ中心部が負圧となる、最小な間隔を隔てて設置する。この筒状体を持つ蓋の筒の外周は、微細気泡を含む液体で満たされており、低速になっているが旋回運動をしており、せん断された気泡の大径の物や一時的に多量に混入した気体は穴が穿孔された筒状の外周に、向心力により、選択的に集まる。小径の微細気泡は液体と共に外周部より外部へ放出される。この集まった気体や大径気泡混じりの液体は、筒の周上の穴に向い、この穴より吸込まれ、再度せん断させる様にしている、また、筒の周上の穴より外部側は円錐状に拡大させ、気体や大径気泡を穴に導く様にし、この穴より吸込まれ、再度せん断させる様にしている、循環流路を備えた、さらに、騒音を低減させる機能を備えた、請求項1乃至2に記載の微細気泡発生装置である。  As shown in FIG. 4, the microbubble generator according to claim 3 of the present invention has an inner diameter with a plurality of holes perforated on the circumference with a rear wall immediately after the outlet for the liquid that rotates at high speed. Install a lid with a cylindrical body that is the same size as the outlet, or a lid with a cylindrical body whose inner diameter is the same as that of the outlet, outside the hole. The gas-liquid that has been formed into a film containing fine bubbles can be passed through, and the central portion is set to be at a negative pressure at a minimum interval. The outer circumference of the cylinder of the lid having this cylindrical body is filled with a liquid containing fine bubbles, and is rotating at a low speed but is swirling, and a large-sized object of sheared bubbles or temporarily The gas mixed in a large amount is selectively collected by the centripetal force on the cylindrical outer periphery in which the holes are perforated. The small-sized fine bubbles are discharged from the outer peripheral portion together with the liquid. The collected gas or liquid mixed with large-diameter bubbles is directed to the hole on the circumference of the cylinder, and is sucked through this hole to be sheared again. Also, the outer side of the hole on the circumference of the cylinder is conical. And a function for reducing noise, further comprising a circulation channel that allows gas or large-diameter bubbles to be introduced into the hole, and is sucked from the hole and sheared again. It is a fine bubble generator as described in 1-2.

本発明の請求項4に記載の微細気泡発生装置は、図5、図6、図7、図8に示すように、液体導入口と予旋回室の間に、液体の流れ方向を変え、予旋回を与える事により、ベーン状ノズルへ液体がより滑らかに且つ均等に液体が導かれる。また、旋回している液体の運動エネルギーが有効に活かされる。この様な、案内ベーンを備えた、請求項1乃至3に記載の微細気泡発生装置である。  As shown in FIGS. 5, 6, 7, and 8, the microbubble generator according to claim 4 of the present invention changes the flow direction of the liquid between the liquid inlet and the pre-swirl chamber, so By giving the swirl, the liquid is more smoothly and evenly guided to the vane-shaped nozzle. Further, the kinetic energy of the swirling liquid is effectively utilized. It is such a microbubble generator of Claims 1 thru | or 3 provided with the guide vane.

本発明の請求項5に記載の微細気泡発生装置は、図9、図10に示すように、主旋回室の後壁の頂部の中心線上の位置に、気体導入口を設け、外部より気体を吸入出来る様に流路を備えた、請求項1乃至4に記載の微細気泡発生装置である。  As shown in FIGS. 9 and 10, the fine bubble generator according to claim 5 of the present invention is provided with a gas inlet at a position on the center line of the top of the rear wall of the main swirl chamber, and gas is supplied from the outside. The microbubble generator according to claim 1, further comprising a flow path so as to allow inhalation.

なお、従来技術では、液体導入口が直接、接線方向で旋回室に、流入する為、高速旋回する液体の中心軸が、供給圧力によって僅かに変動する。その為に、設計圧力より離れた圧力で供給した場合、旋回中心線上に発生した気柱軸が、気体導入口の位置とずれ、吸気不良や、これによる気柱軸の高真空でキャビテーションが発生し、気体導入口付近が侵食されることがある。  In the prior art, since the liquid inlet directly flows into the swirl chamber in the tangential direction, the central axis of the liquid swirling at a high speed slightly varies depending on the supply pressure. For this reason, when the pressure is supplied at a pressure far from the design pressure, the air column shaft generated on the swiveling center line deviates from the position of the gas inlet, and intake failure or cavitation occurs due to the high vacuum of the air column shaft. However, the vicinity of the gas inlet may be eroded.

本発明の請求項6に記載の微細気泡発生装置は、図11、図12、図13、図14に示すように、液体中に加圧溶解された気体の一部は気泡化されないまま放出されており、この溶解された気体を効率良く気泡化する為に、高速旋回する液体の導出口の直後または、請求項3の循環流路構造の直後に、所定の空間を設け、外部側壁に筒状またはコーン状の減圧発泡を促進させる流路を設け、ここで減圧発泡をさせ、微細気泡をより多く発生することができ、さらに、騒音を低減させる機能を備えた、請求項1乃至5に記載の微細気泡発生装置である。  As shown in FIGS. 11, 12, 13, and 14, the microbubble generator according to claim 6 of the present invention releases a part of the gas pressurized and dissolved in the liquid without being bubbled. In order to efficiently bubble the dissolved gas, a predetermined space is provided immediately after the outlet of the liquid that rotates at high speed or immediately after the circulation channel structure according to claim 3, and a cylinder is formed on the outer side wall. A flow path that promotes vacuum-like or corn-like decompression foaming is provided, wherein decompression foaming is performed, more fine bubbles can be generated, and noise reduction is further provided. It is a microbubble generator of description.

本発明の請求項7に記載の微細気泡発生装置は、排水、汚水処理等で使用する場合、ストレーナで完全に捕捉し難い繊維状の異物が、ベーン状ノズルに引っ掛るという問題点を解決するもので、図15に示すように、前壁と後壁の間隔を保ったまま、また図16に示すように、前壁どうしの間隔を保ったまま、ベーン状ノズルの幅を減少させ、前壁側または後壁側あるいは中間に隙間を設け、異物が通過し易くした、請求項1乃至6に記載の微細気泡発生装置である。  The fine bubble generator according to claim 7 of the present invention solves the problem that, when used in drainage, sewage treatment or the like, fibrous foreign matter that is difficult to be completely captured by the strainer is caught by the vane nozzle. As shown in FIG. 15, the width of the vane nozzle is reduced while maintaining the distance between the front wall and the rear wall, and as shown in FIG. 16, while maintaining the distance between the front walls. The fine bubble generating device according to any one of claims 1 to 6, wherein a gap is provided on the wall side, the rear wall side, or in the middle so that foreign substances can easily pass therethrough.

本発明の請求項8に記載の微細気泡発生装置は、請求項3に記載の微細気泡発生装置において、さらに気泡径選択機能と溶解気体の発泡を促進させる機能を持たせるための構造で、図17に示すように、循環用筒状蓋の循環用筒状部の外周に流体による抵抗が無視できる程度の流路面積をもたせる様に径方向に間隙を設けた筒状体を設置し、ここでの旋回角速度を最大となる様にして大小の気泡の選択機能を最大とする。さらに、前記筒状体の外周に同じ様に2つ目の筒状体を設け、流路をジグザグに通し、渦流を発生させる事により、導入された液体中に溶解された溶存気体を、発泡させる。そのために、その筒状体の一端に複数のスリット状、穴状の流路を設けるか、流路分を短くした、1重または2重の円筒状の筒状体を設ける。このスリット、穴、隙間の位置は1重目は導出口の反対側に、2重目は導出口側に設ける。これにより微細気泡をより多く発生することができる。気泡径選択強化機能と溶解気体の発泡を促進させる機能を持たせた、筒状体を組み込んだ、請求項1乃至7に記載の微細気泡発生装置である。  The fine bubble generating device according to claim 8 of the present invention is a structure for providing the fine bubble generating device according to claim 3 with a function of further promoting a bubble diameter selection function and foaming of dissolved gas. As shown in FIG. 17, a cylindrical body provided with a gap in the radial direction is installed on the outer periphery of the circulation cylindrical portion of the circulation cylindrical lid so as to have a flow passage area where the resistance by the fluid is negligible. Maximize the function of selecting large and small bubbles by maximizing the turning angular velocity at. Furthermore, a second cylindrical body is provided on the outer periphery of the cylindrical body in the same manner, and the dissolved gas dissolved in the introduced liquid is foamed by passing the flow path through a zigzag and generating a vortex. Let For this purpose, a plurality of slit-like or hole-like flow paths are provided at one end of the cylindrical body, or a single or double cylindrical tubular body with a reduced flow path is provided. As for the positions of the slits, holes and gaps, the first is provided on the side opposite to the outlet and the second is provided on the outlet. Thereby, more fine bubbles can be generated. The microbubble generator according to any one of claims 1 to 7, which incorporates a cylindrical body having a function of enhancing the bubble diameter selection and a function of promoting foaming of dissolved gas.

本発明の請求項9に記載の微細気泡発生装置は、図18に示すように、後壁部の形状を富士山様から円錐状とし、ベーン状ノズル流入部の流れを鋭角から鈍角とし、乱流の防止と摩擦抵抗の低減を図るべく主旋回室外周部の流れ方向を斜流とした請求項1および請求項3乃至8に記載の微細気泡発生装置である。  As shown in FIG. 18, the fine bubble generator according to claim 9 of the present invention has a shape of the rear wall portion changed from Mt. Fuji to a conical shape, and the flow of the vane-shaped nozzle inflow portion is changed from an acute angle to an obtuse angle, 9. The microbubble generator according to claim 1, wherein the flow direction of the outer periphery of the main swirl chamber is a diagonal flow in order to prevent friction and reduce frictional resistance.

本発明の請求項10に記載の微細気泡発生装置は、図19に示すように、請求項3に記載の微細気泡発生装置において、循環用筒状蓋の循環用筒状部を蓋付の筒状体とし、蓋後壁と軸方向に移動可能となる様に分離し、可撓性と弾性を持った連通部がある支持部材により、初期位置は、運転中の導出口より放出された微細気泡を含む膜状となった気液が通過出来、かつ筒の中心部が負圧となる最小な間隔より、より広く、かつ運転開始で中心部の負圧により、自動で導出口側へ引かれ、運転中は先の最小な間隔となる位置になる位置で、これを固定し、蓋付筒状体の内側と外側の圧力差による軸方向の推力で自動的に隙間調整をして、閉塞防止機能を持たせた、請求項1乃至9に記載の微細気泡発生装置である。  As shown in FIG. 19, the fine bubble generating device according to claim 10 of the present invention is the fine bubble generating device according to claim 3, wherein the circulation cylindrical portion of the circulation cylindrical lid is a cylinder with a lid. It is separated from the rear wall of the lid so that it can move in the axial direction, and the initial position is finely released from the outlet port during operation by a support member with a flexible and elastic communicating part. The gas-liquid in the form of a film containing bubbles can pass through and is automatically drawn to the outlet side by the negative pressure at the center of the tube, which is wider than the minimum interval at which the center of the tube is negative, and at the start of operation. During operation, it is fixed at the position where it becomes the minimum interval, and the gap is automatically adjusted by the axial thrust due to the pressure difference between the inside and outside of the cylindrical body with lid, The microbubble generator according to any one of claims 1 to 9, which has a blocking prevention function.

本発明の請求項11に記載の微細気泡発生装置は、図20に示すように、請求項3に記載の微細気泡発生装置において、循環用筒状蓋と、導出口を備える前壁部分とを磁性体で製作し、外周部等、適切な位置に永久磁石もしくは励磁コイルで磁気回路を構成し、磁気回路の空隙の磁束密度が最大となる導出口部で高速で放出された膜状となった液体中にリング状に発電電流が流れる様にし、活水器機能を持たせた、微細気泡発生を妨害することなく可能となる、請求項1乃至10に記載の微細気泡発生装置である。  As shown in FIG. 20, the fine bubble generating device according to claim 11 of the present invention is the fine bubble generating device according to claim 3, comprising: a cylindrical lid for circulation; and a front wall portion having a lead-out port. It is made of a magnetic material, and a magnetic circuit is configured with a permanent magnet or exciting coil at an appropriate position such as the outer periphery. The film is released at high speed at the outlet port where the magnetic flux density of the air gap in the magnetic circuit is maximized. The microbubble generator according to any one of claims 1 to 10, which enables generation of electric current to flow in a ring shape in a liquid and has a function of a water heater without interfering with microbubble generation.

従来技術での高効率な微細気泡発生装置に比べ約半分のエネルギーで同等で良好な微細気泡を多量に発生させる事ができる為、微細気泡発生システム全体のコンパクト化や低コスト化が可能となる。  Compared to the high-efficiency micro-bubble generator in the prior art, it can generate a large amount of equal and good micro-bubbles with about half the energy, so the entire micro-bubble generator system can be made compact and cost-effective. .

従来技術品に比較し、エネルギー消費が少ないため、ランニングコストも低減される。  Since the energy consumption is lower than that of the prior art products, the running cost is also reduced.

また、導入された液体の流路での流れが滑らかとなる為、低振動となる。  Further, since the flow of the introduced liquid in the flow path becomes smooth, the vibration becomes low.

また、供給液体流量に合わせて、高効率な微細気泡発生装置を設計することが、容易に出来る。  In addition, it is easy to design a highly efficient fine bubble generator in accordance with the flow rate of the supplied liquid.

さらに、蓋等に依る導出口での騒音発生の遮蔽と、ポンプの低圧化に依り低騒音化が可能となり設置場所の制限が少なくなる。  Furthermore, the noise can be reduced by shielding the generation of noise at the outlet through a lid and the like, and lowering the pressure of the pump, and the installation place is reduced.

以下、本発明の実施の形態を説明する。
(実施の形態1)
図1、図2は本発明の請求項1に記載の微細気泡発生装置の一例である。なお、図1は側面の断面図、図2は図1のA−A線断面図である。液体導入口106より加圧された液体、気泡混じりの液体、気体が溶解された液体は、予旋回室105に向けられ導入され、ベーン状ノズル104の外周より滑らかに且つ均等に流れ込む。流れ込んだ液体は薄い帯板状の噴流となり、主旋回室100の外周の接線方向に向け噴出される。噴出された液体は、流速に余分な加速度が発生し難い断面を持った主旋回室100の外周より内周にある導出口103に向かって、旋回が乱れる事無く、旋回角速度を増速させ、導出口103より放出する。また、主旋回室100の中心線上に、気柱軸が発生し、放出時、粘性で気柱軸の気体を引き千切り、巻き込んで磨り潰し、気泡をせん断し、微細気泡を多量に発生させることができる。
Embodiments of the present invention will be described below.
(Embodiment 1)
1 and 2 show an example of a microbubble generator according to claim 1 of the present invention. 1 is a side sectional view, and FIG. 2 is a sectional view taken along the line AA in FIG. The liquid pressurized from the liquid inlet 106, the liquid in which bubbles are mixed, or the liquid in which the gas is dissolved is introduced toward the pre-revolution chamber 105 and flows smoothly and evenly from the outer periphery of the vane nozzle 104. The flowing liquid becomes a thin strip-like jet and is jetted in the tangential direction of the outer periphery of the main swirl chamber 100. The ejected liquid increases the swirl angular velocity without disturbing swirl from the outer periphery of the main swirl chamber 100 having a cross section in which excessive acceleration is unlikely to occur in the flow velocity toward the outlet port 103 in the inner periphery, It discharges from the outlet 103. In addition, an air column axis is generated on the center line of the main swirl chamber 100, and when released, the gas of the air column axis is drawn by viscosity and is shredded, entrained and crushed, the bubbles are sheared, and a large amount of fine bubbles are generated. Can do.

(実施の形態2)
図3は本発明の請求項2に記載の微細気泡発生装置の一例である。なお、図3は側面の断面図である。液体導入口106より加圧された気泡混じりの液体、気体が溶解された液体は、予旋回室105に向けられ導入され、適切な幅を持った、ベーン状ノズル104の外周より滑らかに且つ均等に流れ込む。流れ込んだ液体は薄い帯板状の噴流となり、主旋回室100の外周の接線方向に向け噴出される。噴出された液体は、流速に余分な加速度が発生し難い断面を持った主旋回室100の外周より内周の両側にある導出口103に向かって、旋回が乱れる事無く、旋回角速度を増速させ、2箇所の導出口103より放出する。また、主旋回室100の中心線上に、気柱軸が発生し、放出時、粘性で気柱軸の気体を引き千切り、巻き込んで磨り潰し、気泡をせん断し、微細気泡を多量に発生させることができる。
(Embodiment 2)
FIG. 3 is an example of a microbubble generator according to claim 2 of the present invention. FIG. 3 is a side sectional view. The liquid in which bubbles are mixed and the liquid in which the gas is dissolved, which is pressurized from the liquid inlet 106, is introduced toward the pre-revolving chamber 105, and is smoother and more uniform than the outer periphery of the vane nozzle 104 having an appropriate width. Flow into. The liquid that flows in becomes a thin strip-like jet and is jetted toward the tangential direction of the outer periphery of the main swirl chamber 100. The ejected liquid increases the swirl angular velocity without disturbing swirl from the outer periphery of the main swirl chamber 100 having a cross section in which excessive acceleration is unlikely to be generated to the outlet ports 103 on both sides of the inner periphery. And discharged from two outlets 103. In addition, an air column axis is generated on the center line of the main swirl chamber 100, and when released, the gas in the air column axis is drawn by viscosity and is shredded, crushed and crushed, the bubbles are sheared, and a large amount of fine bubbles are generated. Can do.

(実施の形態3)
図4は本発明の請求項3に記載の微細気泡発生装置の一例である。上記、実施の形態1、実施の形態2の導出口103の直後に付けるものである。なお、図4は側面の断面図である。導出口103より旋回しながら膜状で放出された気泡混じりの液体は、遠心力、向心力にて、小径の微細気泡は外周に寄り、外部へ放出通路より放出され、大径の微細気泡や一時的に多量に混入した気体は内周に寄り、負圧に依り、循環用筒状体200の穴201を通過し矢印の方向に流れ、導出口103側に引き込まれ、再度、高速旋回している液体と合わさり、気泡、気体がせん断され、微細化される。なお、循環用筒状体200の穴201の外部側は円錐状に拡大させ、穴に導く様にしてもよい。
(Embodiment 3)
FIG. 4 is an example of a microbubble generator according to claim 3 of the present invention. This is attached immediately after the outlet 103 of the first and second embodiments. FIG. 4 is a side sectional view. The bubble-mixed liquid that is discharged in the form of a film while swirling from the outlet 103 is centrifugally and centripetally, and the small-sized fine bubbles are moved toward the outer periphery and discharged to the outside from the discharge passage. The gas mixed in a large amount approaches the inner circumference, and depending on the negative pressure, passes through the hole 201 of the circulation tubular body 200, flows in the direction of the arrow, is drawn into the outlet port 103 side, and rotates again at high speed. Together with the liquid, bubbles and gas are sheared and refined. In addition, the outside of the hole 201 of the cylindrical body for circulation 200 may be expanded in a conical shape and guided to the hole.

(実施の形態4)
図5、図6、図7、図8は本発明の請求項4に記載の微細気泡発生装置の一例である。なお、図5は側面の断面図、図6は図5のB−B線断面図、図7は側面の断面図、図8は図7のC−C線断面図である。図5のように、流入方向と放出方向が直線状の場合や図8のように、流入方向と放出方向が直角で図2の様に偏芯していない場合は、液体導入口106より導入された液体、気泡混じりの液体、気体が溶解された液体を予旋回室105に向け、方向変更や、予旋回を与える、案内ベーン300、301を設け、ベーン状ノズル104へ液体がより滑らかに且つ均等に液体が導かれる様にする。
(Embodiment 4)
5, FIG. 6, FIG. 7 and FIG. 8 show an example of the microbubble generator according to claim 4 of the present invention. 5 is a side sectional view, FIG. 6 is a sectional view taken along line BB in FIG. 5, FIG. 7 is a sectional side view, and FIG. 8 is a sectional view taken along line CC in FIG. When the inflow direction and the discharge direction are linear as shown in FIG. 5 or when the inflow direction and the discharge direction are at right angles and are not eccentric as shown in FIG. Guide vanes 300 and 301 are provided for directing the pre-swirl chamber 105 to a direction change or pre-swirl, and the liquid is smoothly supplied to the vane-shaped nozzle 104. In addition, the liquid should be guided evenly.

(実施の形態5)
図9、図10は本発明の請求項5に記載の微細気泡発生装置の一例である。なお、図9、図10は側面の断面図である。主旋回室100の後壁102の頂部の中心線上の位置に、気体導入口400を設け、外部より気体を吸入出来る様に気体導入接続口401を備えており、図22で示す微細気泡発生システム等で使用する。
(Embodiment 5)
9 and 10 show an example of the microbubble generator according to claim 5 of the present invention. 9 and 10 are side sectional views. A fine bubble generating system shown in FIG. 22 is provided with a gas introduction port 400 at a position on the center line of the top of the rear wall 102 of the main swirl chamber 100 and a gas introduction connection port 401 so that gas can be sucked from the outside. Use with etc.

(実施の形態6)
図11、図12、図13図14は本発明の請求項6に記載の微細気泡発生装置の一例である。高速旋回する液体の導出口103の直後または、実施の形態3の循環流路構造の直後に、所定の空間502を設け、外部側壁に筒状通路500またはコーン状流路501の減圧発泡を促進させる流路を設け、ここで減圧発泡をさせ、微細気泡をより多く発生させ、さらに、騒音を低減させる機能を備えている。
(Embodiment 6)
FIG. 11, FIG. 12, FIG. 13 and FIG. 14 show an example of the microbubble generator according to claim 6 of the present invention. A predetermined space 502 is provided immediately after the high-speed swirling liquid outlet 103 or immediately after the circulation flow path structure of the third embodiment to promote decompression foaming of the cylindrical passage 500 or the cone-shaped flow path 501 on the outer side wall. Provided with a function of reducing the noise by providing a flow path for generating a small amount of fine bubbles.

(実施の形態7)
図15、図16は本発明の請求項7に記載の微細気泡発生装置の一例である。ストレーナで捕捉できず通過した繊維状の異物が流入しても、閉塞せずに通過させるもので、性能を低下させる事を抑え、微細気泡を発生できる様にしたものである。導入された液体の流路幅W1を保ったまま、ベーン状ノズル510の幅を減少させ、流入側の形状を先の方を中心側に斜めにし、引っ掛かった異物が移動し、通過する様にしている。また、幅を減少させたベーン状ノズル510は前壁側または後壁側に付けることができる。さらに幅を減少させたベーン状ノズル510を前壁側と後壁側の両方に付け、中央に通過する隙間を設けることができる。この場合、前壁側と後壁側のベーン状ノズル510の回転方向の位置関係を360度/2n(nはベーン状ノズルの数)ずらし、前後が交互とすることが好ましい。
(Embodiment 7)
15 and 16 show an example of the fine bubble generator according to the seventh aspect of the present invention. Even if fibrous foreign matter that cannot be trapped by the strainer flows in, it passes through without blocking, and it is possible to suppress the deterioration of performance and generate fine bubbles. While maintaining the flow path width W1 of the introduced liquid, the width of the vane-shaped nozzle 510 is decreased, the shape on the inflow side is inclined toward the center, and the trapped foreign matter moves and passes. ing. Further, the vane nozzle 510 having a reduced width can be attached to the front wall side or the rear wall side. Furthermore, a vane-like nozzle 510 with a reduced width can be attached to both the front wall side and the rear wall side, and a gap passing through the center can be provided. In this case, it is preferable that the positional relationship in the rotation direction of the vane-shaped nozzles 510 on the front wall side and the rear wall side is shifted by 360 degrees / 2n (n is the number of vane-shaped nozzles), and the front and rear are alternated.

(実施の形態8)
図17は本発明の請求項8に記載の微細気泡発生装置の一例である。請求項3に記載の微細気泡発生装置において、さらに気泡径選択機能と溶解気体の発泡を促進させる機能を持たせるための構造で、循環用筒状蓋200の循環用筒の外周に流体による抵抗が無視できる程度の流路面積をもたせる様に径方向に間隙を設けた筒状体520を設置し、導出口よりの旋回余力を、ここでの旋回角速度を最大となる様に小径化して大小の気泡の選択機能を最大とし大径の気泡を循環用穴201に導く。さらに、前記筒状体520の外周に同じ様に2つ目の筒状体を設け、流路をジグザグに通し、渦流を発生させる事により、導入された液体中に溶解された溶存気体を、発泡させる。そのために、その筒状体520の一端に複数のスリット状、穴状の流路を設けるか、流路分を短くした、1重または2重の円筒状の筒状体520を設ける。このスリット、穴、隙間の位置は1重目は導出口103の反対側に、2重目は導出口103側に設ける。これにより微細気泡をより多く発生することができる。
(Embodiment 8)
FIG. 17 shows an example of a microbubble generator according to claim 8 of the present invention. 4. The fine bubble generating apparatus according to claim 3, further comprising a function for promoting the bubble diameter selection function and the foaming of dissolved gas, and the resistance of the circulation tube of the circulation tube lid 200 to the outer periphery of the circulation tube by a fluid. The cylindrical body 520 having a gap in the radial direction is installed so as to have a flow path area that can be ignored, and the turning remaining force from the outlet is reduced to a maximum so that the turning angular velocity is maximized. The bubble selection function is maximized to guide the large diameter bubble to the circulation hole 201. Furthermore, a second cylindrical body is similarly provided on the outer periphery of the cylindrical body 520, and the dissolved gas dissolved in the introduced liquid is generated by passing the flow path through a zigzag and generating a vortex. Foam. For this purpose, a plurality of slit-like or hole-like flow paths are provided at one end of the cylindrical body 520, or a single or double cylindrical tubular body 520 having a reduced flow path is provided. As for the positions of the slits, holes and gaps, the first is provided on the side opposite to the outlet 103 and the second is provided on the side of the outlet 103. Thereby, more fine bubbles can be generated.

(実施の形態9)
図18は本発明の請求項9に記載の微細気泡発生装置の一例である。後壁102部の形状を富士山様から円錐状後壁530とし、ベーン状ノズル流入部の流れを鋭角から鈍角とし、乱流の防止と摩擦抵抗の低減を図るべく主旋回室外周部の流れ方向を斜流とする。
(Embodiment 9)
FIG. 18 shows an example of a microbubble generator according to claim 9 of the present invention. The shape of the rear wall 102 part is changed from Mt. Fuji to a conical rear wall 530, the flow of the vane nozzle inflow part is changed from an acute angle to an obtuse angle, and the flow direction of the outer periphery of the main swirl chamber is to prevent turbulence and reduce frictional resistance. Is a diagonal flow.

(実施の形態10)
図19は本発明の請求項10に記載の微細気泡発生装置の一例である。請求項3に記載の微細気泡発生装置において、循環用筒状蓋200の循環用筒状部を蓋付の筒状体550とし、蓋後壁と軸方向に移動可能となる様に分離し、可撓性と弾性を持った連通部がある支持部材により、初期位置は、運転中の導出口103より放出された微細気泡を含む膜状となった気液が通過出来、かつ筒の中心部が負圧となる最小な間隔より、より広く、かつ運転開始で中心部の負圧により、自動で導出口103側へ引かれ、運転中は先の最小な間隔となる位置となる位置で、これを固定する。通常運転時はP1=P2>P3となり導出口側へ、異物553がからまった時はP1=P2<P3となり導出口とは反対側に推力が働き筒状体550は移動する。この様に、蓋付筒状体550の内側と外側の圧力差による軸方向の推力で自動的に隙間調整をして、閉塞防止機能を持たせるものである。
(Embodiment 10)
FIG. 19 shows an example of a microbubble generator according to claim 10 of the present invention. In the fine bubble generating device according to claim 3, the cylindrical portion for circulation of the cylindrical lid for circulation 200 is a cylindrical body 550 with a lid, and is separated so as to be movable in the axial direction from the lid rear wall. By the support member having the communication part having flexibility and elasticity, the initial position can pass the gas-liquid in the form of a film containing fine bubbles discharged from the outlet 103 during operation, and the center part of the cylinder Is wider than the minimum interval at which negative pressure is obtained, and is automatically pulled to the outlet 103 side by the negative pressure at the center at the start of operation, and at the position where the minimum interval is reached during operation, Fix this. During normal operation, P1 = P2> P3 is established, and when the foreign object 553 is entangled, P1 = P2 <P3 is established and thrust is applied to the opposite side of the outlet, so that the cylindrical body 550 moves. In this way, the gap is automatically adjusted by the axial thrust due to the pressure difference between the inside and outside of the cylindrical body 550 with a lid, and a blocking prevention function is provided.

(実施の形態11)
図20は本発明の請求項11に記載の微細気泡発生装置の一例である。請求項3に記載の微細気泡発生装置において、循環用筒状蓋200と、導出口103を備える前壁部分とを磁性体で製作し、外周部等、適切な位置に永久磁石540もしくは励磁コイル541にて磁気回路を構成し、磁気回路の空隙の磁束密度が最大となる導出口103部で高速で放出された膜状となった液体中にリング状に発電電流が流れる様にし、活水器機能を持たせた。また形状は変えることがないので微細気泡発生を妨害することなく可能となる。
(Embodiment 11)
FIG. 20 is an example of a microbubble generator according to claim 11 of the present invention. 4. The fine bubble generating apparatus according to claim 3, wherein the circulating cylindrical lid 200 and the front wall portion including the outlet port 103 are made of a magnetic material, and the permanent magnet 540 or the excitation coil is placed at an appropriate position such as an outer peripheral portion. A magnetic circuit is configured at 541, and a power generation current is caused to flow in a ring shape in a film-like liquid discharged at a high speed at the outlet portion 103 where the magnetic flux density of the air gap of the magnetic circuit is maximized. Made it functional. Further, since the shape is not changed, it is possible without disturbing the generation of fine bubbles.

一例として、市販されている、浴槽用微細気泡発生装置で実験を行った結果は次の通りとなった。システムは図23の通りである。
商品構成は300L浴槽用、消費電力430W、気体溶解装置外径115mm高さ210mm(特許第3929472号)、微細気泡発生装置(特許第3682286号)流入圧力0.26MPa、流量12L/分の装置で300L浴槽で微細気泡を発生させた。
これと同じレベルの微細気泡を本発明の微細気泡発生装置と付替え、ポンプ圧力を変更し、同等となる圧力を調べた。その結果、微細気泡発生装置流入圧力0.20MPa、流量7L/分、給気量700CC/分、消費電力260Wとなった。
ここで、微細気泡発生装置に入力されているエネルギーは、水動力として(L=0.163QH(比重1の場合))で計算すると、前者は約51W、後者は約23Wと半分以下となる。また、騒音も聴感上であるが約半減した。
さらに、気泡径を顕微鏡で測定し、クリアー光学製P−100H型ガラススケールの目盛と比較すると、図24の様にサイズは、殆んどの物が40ミクロンから50ミクロンであり、多量に発生しているのが観察できる、量的には概略50万個/CC(5億個/L)とみられる。
なお、実験で使用した微細気泡発生装置の各部の主要寸法他は、予旋回室外径35mm、ベーン状ノズルの幅2mm、ベーン状ノズルの数9箇所、主旋回室外径20mm、導出口径6mm、本体外径50mm、長さ50mmで形状は図14の方式で筒状通路の物で、比較した従来技術の物は旋回室外形約45mm、本体外径約50mm、長さ約100mmで、本考案品は半分の体積となっている。
As an example, the results of an experiment using a commercially available microbubble generator for bathtubs are as follows. The system is as shown in FIG.
The product configuration is for 300L bathtub, power consumption 430W, gas dissolving device outer diameter 115mm height 210mm (patent No. 3929472), fine bubble generator (patent No. 3682286) inflow pressure 0.26MPa, flow rate 12L / min. Fine bubbles were generated in a 300 L bath.
The same level of microbubbles was replaced with the microbubble generator of the present invention, the pump pressure was changed, and the equivalent pressure was examined. As a result, the microbubble generator inflow pressure was 0.20 MPa, the flow rate was 7 L / min, the air supply amount was 700 CC / min, and the power consumption was 260 W.
Here, when the energy input to the microbubble generator is calculated as hydraulic power (L = 0.163QH (in the case of specific gravity 1)), the former is about 51 W and the latter is about 23 W, which is less than half. In addition, noise was reduced by about half, although it was audible.
Furthermore, when the bubble diameter is measured with a microscope and compared with the scale of a clear optical P-100H type glass scale, most of the sizes are 40 to 50 microns as shown in FIG. It can be observed that the quantity is approximately 500,000 / CC (500 million / L).
In addition, the main dimensions of each part of the fine bubble generator used in the experiment include a pre-swirl chamber outer diameter of 35 mm, a vane-shaped nozzle width of 2 mm, nine vane-shaped nozzles, a main swirl chamber outer diameter of 20 mm, a discharge port diameter of 6 mm, a main body The outer diameter is 50 mm, the length is 50 mm, and the shape is a cylindrical passage according to the method shown in FIG. 14, and the comparative prior art is about 45 mm in swirl chamber outer diameter, about 50 mm in outer diameter, and about 100 mm in length. Is half the volume.

また、図9、図10の方式は図22に示すシステム等で使用し、その他の方式は図21、図23に示すシステム等で使用できる。  9 and 10 can be used in the system shown in FIG. 22 and other methods can be used in the system shown in FIGS.

実施形態1の微細気泡発生装置の側面の断面図Sectional drawing of the side surface of the microbubble generator of Embodiment 1 図1におけるA−A線断面図AA line sectional view in FIG. 実施形態2の微細気泡発生装置の側面の断面図Sectional drawing of the side surface of the microbubble generator of Embodiment 2 実施形態3の微細気泡発生装置の側面の断面図Sectional drawing of the side surface of the microbubble generator of Embodiment 3 実施形態4の微細気泡発生装置の側面の断面図Sectional drawing of the side surface of the microbubble generator of Embodiment 4 図5におけるB−B線断面図BB sectional view in FIG. 実施形態4の微細気泡発生装置の側面の断面図Sectional drawing of the side surface of the microbubble generator of Embodiment 4 図7におけるC−C線断面図CC sectional view in FIG. 実施形態5の微細気泡発生装置の側面の断面図Sectional drawing of the side surface of the microbubble generator of Embodiment 5 実施形態5の微細気泡発生装置の側面の断面図Sectional drawing of the side surface of the microbubble generator of Embodiment 5 実施形態6の微細気泡発生装置の側面の断面図Sectional drawing of the side surface of the microbubble generator of Embodiment 6 実施形態6の微細気泡発生装置の側面の断面図Sectional drawing of the side surface of the microbubble generator of Embodiment 6 実施形態6の微細気泡発生装置の側面の断面図Sectional drawing of the side surface of the microbubble generator of Embodiment 6 実施形態6の微細気泡発生装置の側面の断面図Sectional drawing of the side surface of the microbubble generator of Embodiment 6 実施形態7の微細気泡発生装置の側面の断面図Sectional drawing of the side surface of the microbubble generator of Embodiment 7 実施形態7の微細気泡発生装置の側面の断面図Sectional drawing of the side surface of the microbubble generator of Embodiment 7 実施形態8の微細気泡発生装置の側面の断面図Sectional drawing of the side surface of the microbubble generator of Embodiment 8 実施形態9の微細気泡発生装置の側面の断面図Sectional drawing of the side surface of the microbubble generator of Embodiment 9 実施形態10の微細気泡発生装置の側面の断面図Sectional drawing of the side surface of the microbubble generator of Embodiment 10. 実施形態11の微細気泡発生装置の側面の断面図Sectional drawing of the side surface of the microbubble generator of Embodiment 11 ポンプ吸込側より気体を導入する微細気泡発生システムFine bubble generation system that introduces gas from the pump suction side 微細気泡発生装置より気体を導入する微細気泡発生システムMicrobubble generation system that introduces gas from microbubble generator 気体溶解装置を備えた高濃度微細気泡発生システムHigh-concentration microbubble generation system with gas dissolving device 実施例で実験した微細気泡の顕微鏡写真(1目盛50ミクロン)Microscopic photo of fine bubbles tested in the example (one scale 50 microns) 従来技術の微細気泡発生装置の正面の断面図Cross-sectional view of the front of a conventional microbubble generator

符号の説明Explanation of symbols

100主旋回室
101前壁
102後壁
103導出口
104べーン状ノズル
106導入口
200循環用筒状蓋
201循環用穴
202循環用傾斜部
300案内ベーン
301案内ベーン(破線部)
400気体導入口
401気体導入接続口
500筒状流路
501コーン状流路
502空間
510幅を減少させたベーン状ノズル
520筒状体
530円錐状後壁
540永久磁石
541励磁コイル
550蓋付の筒状体
551支持部
552連通穴
553異物
600低速域
601増速域
700微細気泡発生装置
701吸込管路
702ポンプ
703気体導入調節弁
704気体溶解装置
705吐出配管
710実験用300L浴槽または液体槽
711液体槽
100 main swirl chamber 101 front wall 102 rear wall 103 outlet 104 vane nozzle 106 inlet 200 circulation cylindrical lid 201 circulation hole 202 circulation inclined part 300 guide vane 301 guide vane (broken line part)
400 gas introduction port 401 gas introduction connection port 500 cylindrical flow channel 501 conical flow channel 502 space 510 width vane nozzle 520 cylindrical body 530 conical rear wall 540 permanent magnet 541 excitation coil 550 cylinder with lid 551 support portion 552 communication hole 553 foreign material 600 low speed region 601 speed increasing region 700 fine bubble generating device 701 suction pipe 702 pump 703 gas introduction control valve 704 gas dissolving device 705 discharge pipe 710 300 L bathtub or liquid tank 711 for experiment Tank

Claims (11)

旋回室での旋回流速に余分な加速度が生じない様に、ノズルから導出口までの領域に於いて、それぞれの位置で、旋回流1周分の周長と旋回室の幅を乗じた面積が同じになる様に成型された、略、高さの違う富士山の輪郭を二重に重ねて出来る中間の空間様の、前壁、後壁を持ち、その外周は、ノズルの幅に合わせた間隔を隔て設置された主旋回室と、前壁の頂部に当る位置に高速旋回する液体の導出口と、主旋回室の外周に等配に設置された、旋回室外周の接線方向に向け薄い帯板状の噴流を発生する一定速または増速機能を備えた10箇所前後のベーン状ノズルと、さらに、その外周に液体導入口よりベーン状ノズルへ滑らかに且つ均等に液体が導かれる様、円形やボリュート形に成型された予旋回室を備えた、微細気泡発生装置。  The area obtained by multiplying the circumference of the swirling flow by one circumference and the width of the swirling chamber at each position in the area from the nozzle to the outlet so that no extra acceleration is generated in the swirling flow velocity in the swirling chamber. An intermediate space formed by overlapping the outlines of Mt. Fuji, which are almost the same height, formed in the same way, has a front wall and a rear wall, and the outer periphery is spaced according to the width of the nozzle A main swirl chamber installed at a distance, a liquid outlet for high-speed swirling at a position corresponding to the top of the front wall, and a thin band in the tangential direction of the outer periphery of the swirl chamber, which is installed evenly around the outer periphery of the main swirl chamber Circular vane nozzles with about 10 vane nozzles having a constant speed or speed increasing function for generating a plate-like jet, and so that the liquid is smoothly and evenly guided from the liquid inlet to the vane nozzles on the outer periphery. A fine bubble generator with a pre-swirl chamber molded into a volute shape. 請求項1に記載の微細気泡発生装置において、後壁部を取り去り、その面で対称になる様、背中合わせに設置し、結果、導出口は2箇所となり、ベーン状ノズルの方向を統一させ、液体導入口を1箇所とした、主旋回室の空間は、両吸込渦巻ポンプの羽根車の輪郭の形状をした微細気泡発生装置。  2. The fine bubble generating device according to claim 1, wherein the rear wall is removed and installed back to back so as to be symmetric with respect to the surface. As a result, there are two outlets, the directions of the vane nozzles are unified, The space in the main swirl chamber with a single inlet is a fine bubble generator having the shape of the outline of the impeller of both suction centrifugal pumps. 旋回式微細気泡発生装置において、高速旋回する液体の導出口の直後に、せん断された気泡の大径の物を選択的に、再度せん断させる様に、後壁の付いた、周上に複数の穴が穿孔された内径が導出口と同程度の筒状体を持つ蓋、または、その穴より外部側は円錐状に拡大された、上記筒状体を持つ蓋を設置し、導出口より放出された微細気泡を含む膜状となった気液が通過出来、かつ筒の中心部が負圧となる、最小な間隔を隔てて設置した、循環流路を備え、さらに騒音を低減させる機能を備えた、本体付加装置、及びこれを備えた、請求項1乃至2に記載の微細気泡発生装置。  In a swirl type fine bubble generator, a large number of sheared bubbles are selectively sheared again immediately after the outlet of the liquid that swirls at high speed. Install a lid with a cylindrical body whose inner diameter is the same as that of the outlet, or a lid with the cylindrical body that is enlarged conically outside the hole, and discharge from the outlet. A function to reduce noise by providing a circulation channel installed at a minimum interval that allows gas-liquid in the form of a film containing fine bubbles to pass through, and the center of the cylinder to have negative pressure. The main body addition apparatus provided, and the fine bubble generating apparatus of Claim 1 thru | or 2 provided with this. 液体導入口と予旋回室の間に、液体に予旋回を与えるための、案内ベーンを備えた、請求項1乃至3に記載の微細気泡発生装置。  The fine bubble generating device according to any one of claims 1 to 3, further comprising a guide vane between the liquid introduction port and the pre-swirl chamber for imparting a pre-swirl to the liquid. 主旋回室の後壁の頂部の中心線上の位置に、気体導入口を設け、外部より気体を吸入出来る様に流路を備えた、請求項1および請求項3乃至4に記載の微細気泡発生装置。  5. The generation of fine bubbles according to claim 1 and 3 to 4, wherein a gas introduction port is provided at a position on the center line of the top of the rear wall of the main swirl chamber, and a flow path is provided so that gas can be sucked from the outside. apparatus. 高速旋回する液体の導出口の直後または、請求項3の循環流路構造の直後に、所定の空間を設け、外部側壁に筒状またはコーン状の減圧発泡を促進させる流路を設け、さらに、騒音を低減させる機能を備えた、請求項1乃至5に記載の微細気泡発生装置。  Immediately after the outlet of the liquid that swirls at high speed or immediately after the circulation flow path structure of claim 3, a predetermined space is provided, and a flow path that promotes decompression foaming in a cylindrical or corn shape is provided on the outer side wall, The fine bubble generating device according to any one of claims 1 to 5, comprising a function of reducing noise. 請求項1および請求項2に記載の微細気泡発生装置において、請求項1の場合は前壁と後壁の間隔を保ったまま、請求項2の場合は前壁どうしの間隔を保ったまま、ベーン状ノズルの幅を減少させ、前壁側または後壁側あるいは中間に隙間を設け、異物が通過し易くした、請求項1乃至6に記載の微細気泡発生装置。  In the fine bubble generator according to claim 1 and claim 2, in the case of claim 1, the distance between the front wall and the rear wall is maintained, and in the case of claim 2, the distance between the front walls is maintained, The fine bubble generating device according to any one of claims 1 to 6, wherein a width of the vane nozzle is reduced, and a gap is provided on the front wall side, the rear wall side, or in the middle so that foreign matters can easily pass therethrough. 請求項3に記載の微細気泡発生装置において、循環用筒状蓋の循環用筒状部の外周に径方向に所定の隙間を設け、その一端に複数のスリット状、穴状の流路を設けるか、流路分を短くした、1重または2重の円筒状の気泡選択強化機能と溶解気体の発泡を促進させる機能を持たせた、筒状体を組み込んだ、請求項1乃至7に記載の微細気泡発生装置。  4. The microbubble generator according to claim 3, wherein a predetermined gap is provided in a radial direction on an outer periphery of the circulation cylindrical portion of the circulation cylindrical lid, and a plurality of slit-like and hole-like flow paths are provided at one end thereof. Or a cylindrical body incorporating a single or double cylindrical air bubble selective strengthening function and a function of promoting foaming of dissolved gas with a shortened flow path portion. Fine bubble generator. 請求項1に記載の微細気泡発生装置において、後壁部の形状を富士山様から円錐状とし、主旋回室外周部の流れ方向を斜流とした請求項1および請求項3乃至8に記載の微細気泡発生装置。  The fine bubble generator according to claim 1, wherein the shape of the rear wall portion is changed from Mt. Fuji to a conical shape, and the flow direction of the outer peripheral portion of the main swirl chamber is a diagonal flow. Fine bubble generator. 請求項3に記載の微細気泡発生装置において、循環用筒状蓋の循環用筒状部を蓋付の筒状体とし、後壁と軸方向に移動可能となる様に分離し、可撓性と弾性を持った連通部がある支持部材により、初期位置は、運転中の導出口より放出された微細気泡を含む膜状となった気液が通過出来、かつ筒の中心部が負圧となる最小な間隔より、より広く、かつ運転開始で中心部の負圧により、自動で導出口側へ引かれ、運転中は先の最小な間隔となる位置、となる位置で、これを固定し、蓋付筒状体の内側と外側の圧力差による軸方向の推力で自動的に隙間調整をして、閉塞防止機能を持たせた、請求項1乃至9に記載の微細気泡発生装置  4. The microbubble generator according to claim 3, wherein the circulation cylindrical portion of the circulation cylindrical lid is formed as a cylindrical body with a lid, separated from the rear wall so as to be movable in the axial direction, and flexible. By the support member with the elastic communicating part, the initial position can pass the gas-liquid in the form of a film containing fine bubbles discharged from the outlet port during operation, and the central part of the cylinder is negative pressure It is wider than the minimum interval and is automatically pulled to the outlet side by the negative pressure at the center at the start of operation, and is fixed at the position that becomes the minimum interval during operation. The fine bubble generating device according to any one of claims 1 to 9, wherein a gap is automatically adjusted by an axial thrust due to a pressure difference between an inner side and an outer side of a cylindrical body with a lid, and a blocking prevention function is provided. 請求項3に記載の微細気泡発生装置において、循環用筒状蓋と、導出口を備える前壁部分とを磁性体で製作し、外周部等に永久磁石もしくは励磁コイルにて磁気回路を構成し、磁気回路の空隙の磁束密度が最大となる導出口部で高速で放出された膜状となった液体中にリング状に発電電流が流れる様にし、活水器機能を持たせた、請求項1乃至10に記載の微細気泡発生装置。  4. The microbubble generator according to claim 3, wherein the cylindrical cover for circulation and the front wall portion having the outlet are made of a magnetic material, and a magnetic circuit is formed by a permanent magnet or an exciting coil on the outer periphery or the like. The generator current is made to flow in the form of a ring in the film-like liquid discharged at a high speed at the outlet portion where the magnetic flux density of the air gap of the magnetic circuit is maximized, thereby providing an active water function. The fine bubble generator as described in thru | or 10.
JP2008336044A 2007-12-14 2008-12-12 Microbubble generator Active JP4636420B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2008336044A JP4636420B2 (en) 2007-12-14 2008-12-12 Microbubble generator

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2007341781 2007-12-14
JP2008336044A JP4636420B2 (en) 2007-12-14 2008-12-12 Microbubble generator

Related Child Applications (1)

Application Number Title Priority Date Filing Date
JP2010097394A Division JP4678617B2 (en) 2007-12-14 2010-04-01 Additional device for swirling microbubble generator

Publications (2)

Publication Number Publication Date
JP2009160576A true JP2009160576A (en) 2009-07-23
JP4636420B2 JP4636420B2 (en) 2011-02-23

Family

ID=40963794

Family Applications (2)

Application Number Title Priority Date Filing Date
JP2008336044A Active JP4636420B2 (en) 2007-12-14 2008-12-12 Microbubble generator
JP2010097394A Active JP4678617B2 (en) 2007-12-14 2010-04-01 Additional device for swirling microbubble generator

Family Applications After (1)

Application Number Title Priority Date Filing Date
JP2010097394A Active JP4678617B2 (en) 2007-12-14 2010-04-01 Additional device for swirling microbubble generator

Country Status (1)

Country Link
JP (2) JP4636420B2 (en)

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010158680A (en) * 2007-12-14 2010-07-22 Yasumasa Nishiyama Additional device for whirling type fine bubble generation apparatus
JP2011194326A (en) * 2010-03-19 2011-10-06 Institute Of National Colleges Of Technology Japan Bubble generator
CN105475217A (en) * 2015-12-30 2016-04-13 商丘市金桥环保科技有限公司 Super silent fish tank aerator
CN105565448A (en) * 2015-11-27 2016-05-11 忠南大学产学合作团 Microbubble generator
JP2018008223A (en) * 2016-07-14 2018-01-18 株式会社Onr Fine bubble generator
WO2018100915A1 (en) * 2016-11-29 2018-06-07 日東精工株式会社 Microbubble generating nozzle
JP2018089610A (en) * 2016-11-29 2018-06-14 日東精工株式会社 Fine bubble generation nozzle
JP2019198857A (en) * 2018-05-15 2019-11-21 リンナイ株式会社 Gas-liquid mixer
CN110521431A (en) * 2019-07-12 2019-12-03 西安交通大学 A kind of micro-nano bubble generator and oxygen-increasing device
CN113207394A (en) * 2021-05-11 2021-08-06 李振方 Accurate fertilizer applicator for planting traditional Chinese medicinal materials and traditional Chinese medicinal material planting process
CN113598124A (en) * 2021-08-23 2021-11-05 浙江省海洋水产研究所 Aeration equipment for large-scale water area culture
CN116212776A (en) * 2023-04-13 2023-06-06 江苏正丹化学工业股份有限公司 Micro-nano gas-liquid reaction device for liquid phase air oxidation of pseudocumene

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6393152B2 (en) * 2014-10-31 2018-09-19 日東精工株式会社 Microbubble generator
KR101609772B1 (en) * 2015-04-30 2016-04-06 (주)고성에코비젼 Multiple function water of Micro Bubble Type Manufacturing Equipment and Multiple function water of Micro Bubble Type Manufacturing method

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5321804Y1 (en) * 1972-03-25 1978-06-07
JPS54143866U (en) * 1978-03-31 1979-10-05
JPH10328542A (en) * 1997-06-03 1998-12-15 Nippon Steel Corp Method for dissolving quick line and device therefor
JP2006015312A (en) * 2004-07-05 2006-01-19 Karuto Kk Fine bubble generation device and method therefor
JP2006142251A (en) * 2004-11-24 2006-06-08 Nitta Moore Co Fine bubble generator

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4636420B2 (en) * 2007-12-14 2011-02-23 康正 西山 Microbubble generator

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5321804Y1 (en) * 1972-03-25 1978-06-07
JPS54143866U (en) * 1978-03-31 1979-10-05
JPH10328542A (en) * 1997-06-03 1998-12-15 Nippon Steel Corp Method for dissolving quick line and device therefor
JP2006015312A (en) * 2004-07-05 2006-01-19 Karuto Kk Fine bubble generation device and method therefor
JP2006142251A (en) * 2004-11-24 2006-06-08 Nitta Moore Co Fine bubble generator

Cited By (21)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010158680A (en) * 2007-12-14 2010-07-22 Yasumasa Nishiyama Additional device for whirling type fine bubble generation apparatus
JP4678617B2 (en) * 2007-12-14 2011-04-27 康正 西山 Additional device for swirling microbubble generator
JP2011194326A (en) * 2010-03-19 2011-10-06 Institute Of National Colleges Of Technology Japan Bubble generator
CN105565448A (en) * 2015-11-27 2016-05-11 忠南大学产学合作团 Microbubble generator
KR101633234B1 (en) * 2015-11-27 2016-06-23 동명대학교산학협력단 Microbuble generator
CN105475217A (en) * 2015-12-30 2016-04-13 商丘市金桥环保科技有限公司 Super silent fish tank aerator
JP2018008223A (en) * 2016-07-14 2018-01-18 株式会社Onr Fine bubble generator
CN109890493A (en) * 2016-11-29 2019-06-14 日东精工株式会社 Micro air bubble generates nozzle
KR102259060B1 (en) * 2016-11-29 2021-05-31 닛또 세이꼬 가부시키가이샤 Nozzle for generating fine bubbles
KR20190053924A (en) * 2016-11-29 2019-05-20 닛또 세이꼬 가부시키가이샤 Fine bubble generating nozzle
WO2018100915A1 (en) * 2016-11-29 2018-06-07 日東精工株式会社 Microbubble generating nozzle
JP2018089610A (en) * 2016-11-29 2018-06-14 日東精工株式会社 Fine bubble generation nozzle
CN109890493B (en) * 2016-11-29 2021-12-10 日东精工株式会社 Micro-bubble generating nozzle
JP2019198857A (en) * 2018-05-15 2019-11-21 リンナイ株式会社 Gas-liquid mixer
JP7228442B2 (en) 2018-05-15 2023-02-24 リンナイ株式会社 Gas-liquid mixer
CN110521431B (en) * 2019-07-12 2021-11-19 西安交通大学 Micro-nano bubble generator and oxygenation device
CN110521431A (en) * 2019-07-12 2019-12-03 西安交通大学 A kind of micro-nano bubble generator and oxygen-increasing device
CN113207394A (en) * 2021-05-11 2021-08-06 李振方 Accurate fertilizer applicator for planting traditional Chinese medicinal materials and traditional Chinese medicinal material planting process
CN113207394B (en) * 2021-05-11 2022-05-24 湖南栀葆堂中药科技有限公司 Accurate fertilizer applicator for planting traditional Chinese medicinal materials and traditional Chinese medicinal material planting method
CN113598124A (en) * 2021-08-23 2021-11-05 浙江省海洋水产研究所 Aeration equipment for large-scale water area culture
CN116212776A (en) * 2023-04-13 2023-06-06 江苏正丹化学工业股份有限公司 Micro-nano gas-liquid reaction device for liquid phase air oxidation of pseudocumene

Also Published As

Publication number Publication date
JP4636420B2 (en) 2011-02-23
JP4678617B2 (en) 2011-04-27
JP2010158680A (en) 2010-07-22

Similar Documents

Publication Publication Date Title
JP2009160576A (en) Fine air bubble generator
JP6564092B2 (en) Gas-liquid dissolution tank and fine bubble generator
JP5133556B2 (en) Microbubble generator
JPWO2008143319A1 (en) Microbubble generator and method
JP6082348B2 (en) Self-priming centrifugal pump device
JP5573879B2 (en) Microbubble generator
KR20170104351A (en) Apparatus for generating micro bubbles
WO2018117040A1 (en) Device and system for generating gas-liquid containing microbubbles
JP2008119567A (en) Microbubble generation device
JP6022779B2 (en) Self-priming centrifugal pump device
CA2723743C (en) Device for mixing gas into a flowing liquid
CN110891674A (en) Microbubble generating apparatus and microbubble generating method, and shower apparatus and oil-water separating apparatus having the same
JP2005118542A (en) Microbubble generator
JP2010167329A (en) Aeration agitator
KR101292601B1 (en) Micro-bubble generator
KR101130816B1 (en) Flotation tank for rotary injection of nano size bubble
JP4903292B1 (en) Swivel type micro bubble generator
KR100854687B1 (en) Micro bubble system
JP5651829B2 (en) Friction reduction ship and micro bubble generation pump
JP2010029774A (en) Fine bubble generating apparatus
JP4228990B2 (en) Microbubble generator
JP2000051107A (en) Bubble generator
JP2022186540A (en) Pressurized fine bubble-containing water generating device
JP2000210545A (en) Bubble generator
CN112647243A (en) Microbubble shower nozzle and have washing equipment of this microbubble shower nozzle

Legal Events

Date Code Title Description
A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20090206

A871 Explanation of circumstances concerning accelerated examination

Free format text: JAPANESE INTERMEDIATE CODE: A871

Effective date: 20090401

A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20090401

A975 Report on accelerated examination

Free format text: JAPANESE INTERMEDIATE CODE: A971005

Effective date: 20090527

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20090721

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20090916

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20091112

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20100202

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20100401

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20100401

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20100720

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20100918

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20101109

A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20101112

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20161203

Year of fee payment: 6

R150 Certificate of patent or registration of utility model

Ref document number: 4636420

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

Free format text: JAPANESE INTERMEDIATE CODE: R150

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20161203

Year of fee payment: 6

S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313114

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20161203

Year of fee payment: 6

R360 Written notification for declining of transfer of rights

Free format text: JAPANESE INTERMEDIATE CODE: R360

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20161203

Year of fee payment: 6

R370 Written measure of declining of transfer procedure

Free format text: JAPANESE INTERMEDIATE CODE: R370

S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313114

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20161203

Year of fee payment: 6

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250