JP2017225961A - Fine bubble generation nozzle - Google Patents

Fine bubble generation nozzle Download PDF

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JP2017225961A
JP2017225961A JP2016125918A JP2016125918A JP2017225961A JP 2017225961 A JP2017225961 A JP 2017225961A JP 2016125918 A JP2016125918 A JP 2016125918A JP 2016125918 A JP2016125918 A JP 2016125918A JP 2017225961 A JP2017225961 A JP 2017225961A
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liquid
flow path
swirl
fine bubble
turning
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JP6842249B2 (en
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清 廣瀬
Kiyoshi Hirose
清 廣瀬
和行 大槻
Kazuyuki Otsuki
和行 大槻
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Nitto Seiko Co Ltd
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Nitto Seiko Co Ltd
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Abstract

PROBLEM TO BE SOLVED: To provide a fine bubble generation nozzle having a significantly enhanced generation rate of fine bubbles at micro- and nano-levels.SOLUTION: The present invention provides a fine bubble generation nozzle 1 comprising a flow passage 11 into which liquid L flows, a turning turbulent flow generating portion 40 for turning the liquid L in the flow passage 11 and generating a turbulent flow in the turning liquid L, and an injection port 31 for injecting the turned liquid L. A turning flow passage 43 of the turning turbulent flow generating portion 40 is formed in a step shape. Since the turbulent flow is generated in the turning liquid L by such a configuration, a large quantity of vortexes are generated. Thus, fine bubbles of micro-level and nano-level are generated in large quantities by injecting the turning liquid L that contains a large quantity of vortexes.SELECTED DRAWING: Figure 1

Description

本発明は、旋回流方式により微細気泡を発生する微細気泡発生ノズルに関する。   The present invention relates to a fine bubble generating nozzle that generates fine bubbles by a swirling flow method.

従来、旋回流方式の微細気泡発生ノズルの一例として、特許文献1に開示されたものがある。従来の微細気泡発生ノズルは、一端に液体を導入する導入口を有するとともに、他端に液体を導出する導出口を有する筒状のケーシング体内に、ケーシング体の周壁に開口した吸気口から気体を導入して液体と混合させる気液混合部と、気液混合体を旋回流となす旋回流形成部とを備えている。旋回流となった気液混合体は、放出される際に強い回転の影響で横にはじき飛ばされる力を受け、気体が渦の崩壊に伴ってねじりと引っ張りの作用を受けて分断される。このようにして分断化されることにより、微細気泡が生成される。   Conventionally, as an example of a swirl flow type fine bubble generating nozzle, there is one disclosed in Patent Document 1. A conventional fine bubble generating nozzle has an inlet for introducing liquid at one end and a gas from an intake port opened on the peripheral wall of the casing body into a cylindrical casing body having an outlet for discharging liquid at the other end. The gas-liquid mixing part which introduces and mixes with the liquid and the swirl flow formation part which makes a gas-liquid mixture turn into a swirl flow are provided. The gas-liquid mixture that has turned into a swirl is subjected to a force that is repelled sideways by the influence of strong rotation when released, and the gas is divided by the action of twisting and pulling as the vortex breaks down. By being divided in this manner, fine bubbles are generated.

特 開 2 0 0 7 − 2 1 3 4 3号公報Japanese Patent Publication No. 20 07-7 1 3 4 3

しかしながら、従来の微細気泡発生ノズルでは、マイクロレベル(数十〜数百μm)およびナノレベル(1μm未満)の気泡の発生割合が低く、マイクロレベル以下の気泡が求められる産業分野に活用できない問題を有していた。   However, the conventional fine bubble generating nozzle has a low generation rate of micro-level (several tens to several hundreds of μm) and nano-level (less than 1 μm) bubbles, and cannot be utilized in industrial fields where bubbles below the micro level are required. Had.

本発明は、上記問題に鑑みて創生されたものであり、マイクロレベルおよびナノレベルの微細気泡の発生割合を大幅に高めた微細気泡発生ノズルを提供することを目的とする。   The present invention has been created in view of the above problems, and an object of the present invention is to provide a fine bubble generating nozzle that greatly increases the generation ratio of micro-level and nano-level fine bubbles.

液体が流入する流路と、前記流路内の液体を旋回させるとともに、旋回中の液体に乱流を生じさせる旋回乱流発生部と、旋回した液体を噴射する噴射口とを備える微細気泡発生ノズルによる。   Microbubble generation comprising: a flow channel into which liquid flows, a swirling turbulent flow generating unit that swirls the liquid in the flow channel and generates turbulent flow in the swirling liquid, and an ejection port that ejects the swirling liquid By nozzle.

なお、前記旋回乱流発生部は、流路の内部に配設される中子であって、その表面に旋回流路が形成されているが好ましい。   In addition, it is preferable that the swirl turbulent flow generation part is a core disposed inside the flow path, and a swirl flow path is formed on the surface thereof.

なお、前記中子は、略円錐形状であって、その側面および底面に旋回流路が形成されており、頂部を上流側に向けて流路の内部に配設されていることが好ましい。   In addition, it is preferable that the said core is a substantially cone shape, and the turning flow path is formed in the side surface and the bottom face, and it arrange | positions inside the flow path toward the upstream.

なお、前記旋回流路の内面は段形状であることが好ましい。   The inner surface of the swirling channel is preferably stepped.

なお、前記噴射口には気泡切断部が連接してあり、この気泡切断部は、噴射口から噴射した液体が通過可能な孔を複数有することが好ましい。   In addition, it is preferable that a bubble cutting part is connected to the ejection port, and the bubble cutting part has a plurality of holes through which the liquid ejected from the ejection port can pass.

本発明によれば、マイクロレベルおよびナノレベルの微細気泡を大量に発生可能な微細気泡生成ノズルを提供することができる。   ADVANTAGE OF THE INVENTION According to this invention, the micro bubble production | generation nozzle which can generate | occur | produce a large quantity of micro level and nano level micro bubbles can be provided.

本発明の実施形態を示した微細気泡発生ノズルの正面視の縦断面図である。It is a longitudinal cross-sectional view of the front view of the fine bubble generation | occurrence | production nozzle which showed embodiment of this invention. 本発明の実施形態を示した微細気泡発生ノズルの中子の平面図である。It is a top view of the core of a fine bubble generating nozzle showing an embodiment of the present invention. 本発明の実施形態を示した微細気泡発生ノズルの中子の平面側からの斜視図である。It is a perspective view from the plane side of the core of the fine bubble generating nozzle showing the embodiment of the present invention. 本発明の実施形態を示した微細気泡発生ノズルの中子の底面図である。It is a bottom view of a core of a fine bubble generating nozzle showing an embodiment of the present invention. 本発明の実施形態を示した微細気泡発生ノズルの中子の底面側からの斜視図である。It is a perspective view from the bottom face side of the core of the fine bubble generating nozzle showing the embodiment of the present invention. 本発明の実施形態を示した微細気泡発生ノズルの中子を取り除いた状態を示す正面視の縦断面図である。It is a longitudinal cross-sectional view of the front view which shows the state which removed the core of the fine bubble generation | occurrence | production nozzle which showed embodiment of this invention.

以下、図面に基づいて本発明の実施形態を説明する。図1において、1は、微細気泡発生ノズルであり、流入口21から噴射口31へと連通する流路11が形成されたノズル本体10を有している。ノズル本体10は、流入管20と噴射管30とを接続して成る。   Hereinafter, embodiments of the present invention will be described with reference to the drawings. In FIG. 1, reference numeral 1 denotes a fine bubble generating nozzle having a nozzle body 10 in which a flow path 11 communicating from an inlet 21 to an injection port 31 is formed. The nozzle body 10 is formed by connecting an inflow pipe 20 and an injection pipe 30.

前記流入管20は、両端に流入口21および接続口22を備えており、流入口21から接続口22へ向かうにしたがって内径が漸次細径となる流入室23が成形されている。   The inflow pipe 20 includes an inlet 21 and a connection port 22 at both ends, and an inflow chamber 23 whose inner diameter gradually becomes smaller from the inflow port 21 toward the connection port 22 is formed.

前記噴射管30は、両端に接続口32および噴射口31を備えており、接続口32から噴射口31へ向かうにしたがって途中までは内径が漸次拡径となるとともに、途中からは内径が漸次細径となる旋回室33が形成されている。   The injection pipe 30 is provided with a connection port 32 and an injection port 31 at both ends. The inner diameter gradually increases from the connection port 32 toward the injection port 31 and gradually increases from the middle. A swirl chamber 33 having a diameter is formed.

前記流路11は、流入管20の接続口21と、噴射管30の接続口31とを接続して、流入室23と旋回室33とを連通させることにより、流入口21から流入する液体Lを噴射口31から噴出するように構成されいている。流体Lは、酸素、オゾン等の気体を十分に溶解させた加圧溶解液である。また、ノズル本体10には、流路11に交差する吸気孔2が穿設されており、旋回室33に流入する前の液体Lに気体Gを混合するように構成されている。   The flow path 11 connects the connection port 21 of the inflow pipe 20 and the connection port 31 of the injection pipe 30 so that the inflow chamber 23 and the swirl chamber 33 communicate with each other. Is ejected from the ejection port 31. The fluid L is a pressurized solution in which a gas such as oxygen or ozone is sufficiently dissolved. Further, the nozzle body 10 has an intake hole 2 that intersects the flow path 11, and is configured to mix the gas G with the liquid L before flowing into the swirl chamber 33.

前記噴射管30の旋回室33の内部には、旋回乱流発生部として中子40が配設されている。中子40は、略円錐形状(具体的には栗形状)に成形されており、その側面41が旋回室33の内壁において漸次拡径になっている部分33aに沿うように形成されている。また、底面44は、旋回室33の内壁において漸次細径になっている部分33bに沿うように形成されている。このため、中子40は、頂部42を上流側へ向け、旋回室33の内部に嵌合させるように配設されている。   Inside the swirl chamber 33 of the injection pipe 30, a core 40 is disposed as a swirl turbulence generator. The core 40 is formed in a substantially conical shape (specifically, a chestnut shape), and the side surface 41 is formed along a portion 33 a that gradually increases in diameter on the inner wall of the swirl chamber 33. In addition, the bottom surface 44 is formed along a portion 33 b that gradually decreases in diameter on the inner wall of the swirl chamber 33. For this reason, the core 40 is disposed so that the top portion 42 faces the upstream side and is fitted into the inside of the swirl chamber 33.

図2および図3に示すように、平面視において、中子40の側面41には、所定の旋回角度で時計回りに方向転換する上流側羽根部43dが突設されており、同様の上流側羽根部43aが等間隔に六本配置されている。そして、隣接する上流側羽根部43d間の隙間によって、上流側旋回流路43が形成されている。   As shown in FIGS. 2 and 3, in a plan view, an upstream blade portion 43 d that changes the direction clockwise at a predetermined turning angle protrudes from the side surface 41 of the core 40. Six blade portions 43a are arranged at equal intervals. And the upstream turning flow path 43 is formed of the clearance gap between the adjacent upstream blade | wing parts 43d.

前記上流側旋回流路43は、底面43bと、内側側面43cと、外側側面43dとを備えており、中子40を旋回室33の内部に配設したとき、底面43bに対向する上流側旋回流路43の開口部分は、噴射管30の旋回室33の内壁33aによって閉ざされる。要するに、上流側旋回流路43の内面は、底面43b、内側側面43c、外側側面43dおよび旋回室33の内壁33aの四面によって構成されている。このため、上流側旋回流路43には、図3の二点鎖線で示すように液体Lが流れ、上流側旋回流路43は、流入室23を通過して流れ込んだ液体Lに対し、旋回方向の速度成分を生じさせるように構成されている。   The upstream swirl flow path 43 includes a bottom surface 43b, an inner side surface 43c, and an outer side surface 43d, and when the core 40 is disposed inside the swirl chamber 33, the upstream swirl facing the bottom surface 43b. The opening portion of the flow path 43 is closed by the inner wall 33 a of the swirl chamber 33 of the injection pipe 30. In short, the inner surface of the upstream-side swirl flow path 43 is constituted by four surfaces: a bottom surface 43 b, an inner side surface 43 c, an outer side surface 43 d, and an inner wall 33 a of the swirl chamber 33. For this reason, the liquid L flows through the upstream swirling flow path 43 as shown by a two-dot chain line in FIG. 3, and the upstream swirling flow path 43 swirls with respect to the liquid L flowing through the inflow chamber 23. It is configured to generate a velocity component in the direction.

また、上流側旋回流路43の内面のうち、底面43bおよび外側側面43dは、液体Lの流れる方向に対して段差を有するように、複数の段部を有する段形状に形成されており、ここを流れる液体Lに乱流を生じることによって渦流が生じるように構成されている。なお、上流側旋回流路の内側側面43cは、液体Lの旋回方向の内側に位置するので流量が少なく、渦流の発生に期待できないため、中子の加工効率に鑑みて段形状に形成していない。   Further, among the inner surface of the upstream swirl flow path 43, the bottom surface 43b and the outer side surface 43d are formed in a step shape having a plurality of step portions so as to have a step with respect to the direction in which the liquid L flows. The vortex is generated by generating a turbulent flow in the liquid L flowing through. Note that the inner side surface 43c of the upstream side swirl passage is located inside the swirl direction of the liquid L, and therefore has a low flow rate and cannot be expected to generate a vortex. Therefore, the inner side surface 43c is formed in a step shape in consideration of the machining efficiency of the core. Absent.

また、図6に示すように、上流側旋回流路43の内面のうち、噴射管30の旋回室33の内壁33a(つまり上流側旋回流路43の上面)は、底面43bおよび外側側面43dと同様に、液体Lの流れる方向に対して段差を有するように、複数の段部を有する段形状に形成されている。   As shown in FIG. 6, the inner wall 33a of the swirl chamber 33 of the injection pipe 30 (that is, the upper surface of the upstream swirl flow path 43), among the inner surfaces of the upstream swirl flow path 43, has a bottom surface 43b and an outer side surface 43d. Similarly, it is formed in a step shape having a plurality of step portions so as to have a step in the flowing direction of the liquid L.

また、図3に示すように、上流側旋回流路43の入口Aおよび出口Bは、入口Aの溝深さが出口Bの溝深さよりも深く、かつ入口Aの開口面積が出口Bの開口面積より大きくなるように構成されている。   Further, as shown in FIG. 3, the inlet A and outlet B of the upstream side swirl flow path 43 are such that the groove depth of the inlet A is deeper than the groove depth of the outlet B, and the opening area of the inlet A is the opening of the outlet B. It is comprised so that it may become larger than an area.

図4および図5に示すように、底面視において、前記中子40の底面44には、所定の旋回角度で時計回りに方向転換する下流側羽根部45a,45bが突設されている。下流側羽根部45aと下流側羽根部45bとでは、旋回角度が異なり、旋回角度の異なる下流側羽根部45a,45bが所定の間隔をおいて交互に六本配置されている。そして、隣接する下流側羽根部45aと下流側羽根部45bとの隙間によって、液体Lの流路としての下流側旋回流路45が形成されている。   As shown in FIGS. 4 and 5, when viewed from the bottom, on the bottom surface 44 of the core 40, downstream blade portions 45a and 45b that project clockwise at a predetermined turning angle project. The downstream blade portion 45a and the downstream blade portion 45b have different turning angles, and the downstream blade portions 45a and 45b having different turning angles are alternately arranged at predetermined intervals. A downstream swirl flow path 45 as a flow path for the liquid L is formed by a gap between the adjacent downstream blade section 45a and the downstream blade section 45b.

中子40を旋回室33の内部に配設したとき、前記下流側旋回流路45は、その底面44に対向する開口部分が旋回室33の内壁33bによって閉ざされるように構成されている。このため、下流側旋回流路45には、図5の二点鎖線で示すように液体Lが流れ、下流側旋回流路45は、上流側旋回流路43を通過して流れ込んだ液体Lに対し、さらに旋回方向の速度成分を生じさせるように構成されている。   When the core 40 is disposed inside the swirl chamber 33, the downstream swirl passage 45 is configured such that the opening portion facing the bottom surface 44 is closed by the inner wall 33 b of the swirl chamber 33. For this reason, the liquid L flows through the downstream swirl flow path 45 as shown by the two-dot chain line in FIG. 5, and the downstream swirl flow path 45 flows into the liquid L flowing through the upstream swirl flow path 43. On the other hand, it is further configured to generate a velocity component in the turning direction.

また、中子40の底面44の中央部分には、窪み46が形成されており、この窪み46によって負圧を生じさせることにより、液体Lの旋回力を高めるように構成されている。このように、中子40の側面41に形成された上流側旋回流路43と、中子40の底面44に形成された下流側旋回流路45とによって、中子40の表面には旋回流路が構成されている。   In addition, a recess 46 is formed in the central portion of the bottom surface 44 of the core 40, and a negative pressure is generated by the recess 46 so that the turning force of the liquid L is increased. Thus, the upstream swirl flow path 43 formed on the side surface 41 of the core 40 and the downstream swirl flow path 45 formed on the bottom surface 44 of the core 40 cause a swirl flow on the surface of the core 40. A road is constructed.

図1に示すように、前記噴射口には気泡切断部50が連接してある。この気泡切断部50は、両端開口の筒状であり、側面に複数の孔が穿設されている。噴射口31から噴射された液体Lは、気泡切断部50の筒内を通過するが、気泡切断部50の一端は蓋体51によって閉じられているため、液体Lは、気泡切断部50の側面に形成された孔を通過して外部に流出する。そして、蓋体51に穿設された吐出口52から噴射される。   As shown in FIG. 1, a bubble cutting part 50 is connected to the injection port. The bubble cutting part 50 has a cylindrical shape with openings at both ends, and a plurality of holes are formed in the side surface. The liquid L ejected from the ejection port 31 passes through the inside of the bubble cutting unit 50, but since the one end of the bubble cutting unit 50 is closed by the lid 51, the liquid L is the side surface of the bubble cutting unit 50. It flows out through the hole formed in the outside. And it ejects from the discharge port 52 drilled in the cover body 51.

以上のように、構成された微細気泡発生のノズルの基本動作を説明する。   The basic operation of the nozzle for generating fine bubbles as described above will be described.

流入口21から流入した液体Lは、流入室23を流れ、流入管20と噴射管30の接続部分付近で、吸気口2から空気Gが混合される。旋回室23に流入した液体Lは、上流側旋回流路43および下流側旋回流45へ流れ込むことにより旋回流となる。ここで、上流側旋回流路43の内面が段形状になっていることにより、乱流が生じる。このとき、大量の渦が発生する。しかも、上流側旋回流路43の断面積は、入口Aから出口Bにかけて徐々に小さくなるため、発生する渦のサイズは非常に小さくなる。このような構成により、小さな渦を大量に含んだ旋回流を生成することが可能になる。こうして、旋回流となった液体Lは、噴射口31から噴射される。このとき、放出される際に強い回転の影響で横にはじき飛ばされる力を受け、気体が渦の崩壊に伴ってねじりと引っ張りの作用を受けて分断される。分断化されることにより、微細気泡が生成される。さらに、噴射口31には、気泡切断部50が連接してあるため、微細気泡がさらに微細化される。このように、大量の渦を含む状態で旋回する液体Lを噴射することにより、マイクロレベルおよびナノレベルの微細気泡が大量に生成される。   The liquid L flowing in from the inflow port 21 flows through the inflow chamber 23, and the air G is mixed from the intake port 2 in the vicinity of the connection portion between the inflow tube 20 and the injection tube 30. The liquid L that has flowed into the swirl chamber 23 flows into the upstream swirl flow path 43 and the downstream swirl flow 45 to become a swirl flow. Here, since the inner surface of the upstream side swirl flow path 43 has a step shape, a turbulent flow is generated. At this time, a large amount of vortices are generated. Moreover, since the cross-sectional area of the upstream-side swirl passage 43 gradually decreases from the inlet A to the outlet B, the size of the generated vortex becomes very small. Such a configuration makes it possible to generate a swirling flow containing a large amount of small vortices. Thus, the liquid L that has become a swirling flow is ejected from the ejection port 31. At this time, when it is released, it receives a force that is blown sideways by the influence of strong rotation, and the gas is divided by the action of twisting and pulling as the vortex breaks down. By dividing, fine bubbles are generated. Furthermore, since the bubble cutting part 50 is connected to the injection port 31, the fine bubbles are further refined. Thus, by ejecting the liquid L that swirls in a state including a large amount of vortices, a large amount of micro-level and nano-level fine bubbles are generated.

なお、前記上流側旋回流路43の内面は、段形状に限定されるものではなく、例えば、複数の窪み部を有するティンプル形状や、複数の突部を備える構成であってよい。このような構成であっても、上流側旋回流路43を流れる液体Lに乱流を生じさせて大量の渦流を発生させることは可能である。また、上流側旋回流路43の内面において、段形状に形成する面は、上記の実施形態に限定されるものではなく、四面のいずれかを段形状にすればよい。   In addition, the inner surface of the upstream swirl flow path 43 is not limited to a step shape, and may be a configuration including a timple shape having a plurality of depressions and a plurality of protrusions, for example. Even with such a configuration, it is possible to generate a turbulent flow in the liquid L flowing through the upstream-side swirl passage 43 to generate a large amount of vortex. Moreover, the surface formed in a step shape on the inner surface of the upstream-side swirl passage 43 is not limited to the above-described embodiment, and any one of the four surfaces may be formed in a step shape.

1 微細気泡発生ノズル
10 ノズル本体
11 流路
21 流入口
31 噴射口
40 中子(旋回乱流発生部)
43 上流側旋回流路
45 下流側旋回流路
50 気泡切断部
DESCRIPTION OF SYMBOLS 1 Fine bubble generation | occurrence | production nozzle 10 Nozzle main body 11 Flow path 21 Inlet 31 Injection port 40 Core (rotating turbulent flow generation part)
43 Upstream swirl flow path 45 Downstream swirl flow path 50 Bubble cutting part

Claims (5)

液体が流入する流路と、
前記流路内の液体を旋回させるとともに、旋回中の液体に乱流を生じさせる旋回乱流発生部と、
旋回した液体を噴射する噴射口と、
を備えることを特徴とする微細気泡発生ノズル。
A flow path for the liquid to flow in;
A swirl turbulence generator that swirls the liquid in the flow path and generates turbulence in the swirling liquid;
An ejection port for ejecting the swirling liquid;
A fine bubble generating nozzle comprising:
前記旋回乱流発生部は、流路の内部に配設される中子であって、その表面に旋回流路が形成されていることを特徴とする請求項1に記載の微細気泡発生ノズル。   2. The fine bubble generating nozzle according to claim 1, wherein the swirling turbulent flow generation portion is a core disposed inside a flow path, and a swirling flow path is formed on a surface thereof. 前記中子は、略円錐形状であって、その側面および底面に旋回流路が形成されており、頂部を上流側に向けて流路の内部に配設されていることを特徴とする請求項2に記載の微細気泡発生ノズル。   The core has a substantially conical shape, and a swirl flow path is formed on a side surface and a bottom surface of the core, and the core is disposed inside the flow path with the top portion facing the upstream side. 2. A fine bubble generating nozzle according to 2. 前記旋回流路の内面は段形状であることを特徴とする請求項2又は3に記載の微細気泡発生ノズル。   4. The fine bubble generating nozzle according to claim 2, wherein an inner surface of the swirl passage has a step shape. 前記噴射口には気泡切断部が連接してあり、この気泡切断部は、噴射口から噴射した液体が通過可能な孔を複数有することを特徴とする請求項1ないし4の何れかに記載の微細気泡発生ノズル。
5. The bubble cutting part is connected to the injection port, and the bubble cutting part has a plurality of holes through which the liquid injected from the injection port can pass. Fine bubble generating nozzle.
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