JP7316006B1 - Fluid mixing device - Google Patents
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- JP7316006B1 JP7316006B1 JP2022201813A JP2022201813A JP7316006B1 JP 7316006 B1 JP7316006 B1 JP 7316006B1 JP 2022201813 A JP2022201813 A JP 2022201813A JP 2022201813 A JP2022201813 A JP 2022201813A JP 7316006 B1 JP7316006 B1 JP 7316006B1
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- 239000012530 fluid Substances 0.000 title claims abstract description 185
- 230000004888 barrier function Effects 0.000 claims abstract description 18
- 230000001105 regulatory effect Effects 0.000 claims abstract description 3
- 239000007788 liquid Substances 0.000 claims description 45
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 31
- 230000015556 catabolic process Effects 0.000 claims description 13
- 238000005192 partition Methods 0.000 claims description 9
- 239000007921 spray Substances 0.000 claims description 5
- 230000002093 peripheral effect Effects 0.000 claims description 3
- 239000007789 gas Substances 0.000 description 17
- 239000000203 mixture Substances 0.000 description 7
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 3
- 239000000446 fuel Substances 0.000 description 3
- 239000003502 gasoline Substances 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 239000003595 mist Substances 0.000 description 2
- 239000001294 propane Substances 0.000 description 2
- 238000009987 spinning Methods 0.000 description 2
- 238000004581 coalescence Methods 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000004080 punching Methods 0.000 description 1
- 230000006798 recombination Effects 0.000 description 1
- 238000005215 recombination Methods 0.000 description 1
- 239000008399 tap water Substances 0.000 description 1
- 235000020679 tap water Nutrition 0.000 description 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/21—Mixing gases with liquids by introducing liquids into gaseous media
- B01F23/213—Mixing gases with liquids by introducing liquids into gaseous media by spraying or atomising of the liquids
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
- B01F23/232—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
- B01F23/232—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles
- B01F23/2326—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles adding the flowing main component by suction means, e.g. using an ejector
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
- B01F23/237—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids characterised by the physical or chemical properties of gases or vapours introduced in the liquid media
- B01F23/2373—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids characterised by the physical or chemical properties of gases or vapours introduced in the liquid media for obtaining fine bubbles, i.e. bubbles with a size below 100 µm
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/10—Mixing by creating a vortex flow, e.g. by tangential introduction of flow components
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/30—Injector mixers
- B01F25/31—Injector mixers in conduits or tubes through which the main component flows
- B01F25/315—Injector mixers in conduits or tubes through which the main component flows wherein a difference of pressure at different points of the conduit causes introduction of the additional component into the main component
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/40—Static mixers
- B01F25/45—Mixers in which the materials to be mixed are pressed together through orifices or interstitial spaces, e.g. between beads
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/40—Static mixers
- B01F25/45—Mixers in which the materials to be mixed are pressed together through orifices or interstitial spaces, e.g. between beads
- B01F25/452—Mixers in which the materials to be mixed are pressed together through orifices or interstitial spaces, e.g. between beads characterised by elements provided with orifices or interstitial spaces
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/70—Spray-mixers, e.g. for mixing intersecting sheets of material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/20—Measuring; Control or regulation
- B01F35/22—Control or regulation
- B01F35/221—Control or regulation of operational parameters, e.g. level of material in the mixer, temperature or pressure
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/71—Feed mechanisms
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/75—Discharge mechanisms
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Dispersion Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Nanotechnology (AREA)
- Accessories For Mixers (AREA)
Abstract
【課題】 旋回流を構成する媒体と異なる媒体中に放出した場合であっても、旋回している流体中に他の流体を微細にして混合する事のできる流体混合装置を提供する。【解決手段】 主流体中に副流体を分散混入させる流体混合装置であって、縦断面形状が円形の内壁面を有する主容器を備えており、当該主容器の内壁面には、その内周面に沿って主流体を案内する主流体導入口が設けられると共に、当該主容器の一方の端部には、当該主容器の軸心方向に副流体を案内する副流体導入口が設けられており、前記主容器における前記副流体導入口が設けられた側とは反対側に存在する他端部には、主容器内で渦流となった主流体を導出する導出口が設けられており、当該導出口の外側には、導出される流体に対する圧力障壁を形成する圧力調整部を設けた流体混合装置とする。【選択図】図3Kind Code: A1 A fluid mixing device capable of finely mixing other fluid into a swirling fluid even when discharged into a medium different from the medium forming the swirling flow. SOLUTION: This fluid mixing device disperses and mixes a secondary fluid in a main fluid, and includes a main container having an inner wall surface having a circular vertical cross-sectional shape. A main fluid introduction port is provided for guiding the main fluid along the surface, and a secondary fluid introduction port is provided at one end of the main container for guiding the secondary fluid in the axial direction of the main container. and an outlet port for leading out the main fluid that has become a swirling flow in the main container is provided at the other end of the main container that is located on the side opposite to the side where the secondary fluid inlet port is provided, The fluid mixing device is provided with a pressure regulating section that forms a pressure barrier against the fluid to be discharged outside the outlet. [Selection drawing] Fig. 3
Description
本発明は液体と気体を混合するマイクロバブル発生装置などのように、2つの流体を混合して導出する流体混合装置に関する。 The present invention relates to a fluid mixing device that mixes and derives two fluids, such as a microbubble generator that mixes liquid and gas.
従来、気体を微細な状態にして液体中に導入する装置としてマイクロバブル発生装置が提供されており、液体の旋回流によって気体を撹拌混入させる装置として旋回式微細気泡発生装置が提供されている。 Conventionally, a microbubble generator has been provided as a device for introducing gas into a liquid in a fine state, and a swirling microbubble generator has been provided as a device for stirring and mixing gas by a swirling flow of a liquid.
かかる旋回式微細気泡発生装置については、特許文献1(特開2011-88045号公報)において、液体中へ微細気泡を拡散する形状と微細気泡の発生量を任意に制御可能な旋回式微細気泡発生装置が提案されている。即ち、一端側が壁体で閉口され、他端側が開口している円筒形容器本体の他端側開口部から微細気泡を含む旋回気液混合液を導出する旋回式微細気泡発生装置が提案されている。 Regarding such a spinning microbubble generator, Patent Document 1 (Japanese Patent Application Laid-Open No. 2011-88045) describes a spinning microbubble generator capable of arbitrarily controlling the shape of diffusing microbubbles in a liquid and the amount of microbubbles generated. A device has been proposed. That is, there has been proposed a swirling microbubble generator for leading out a swirling gas-liquid mixture containing microbubbles from an opening on the other end of a cylindrical container body, one end of which is closed by a wall and the other end of which is open. there is
また特許文献2(特開2012-239953号公報)では、小規模な水環境への適用可能なように小型化・簡易化した旋回式微細気泡発生装置として、中空部を有する略球形の器体内に流入した液体の旋回流により気体導入口から自吸した気体を微細気泡化し、気液噴出口から微細気泡を含む旋回気液混合液を導出するように成した旋回式微細気泡発生装置が提案されている。 Further, in Patent Document 2 (Japanese Patent Application Laid-Open No. 2012-239953), as a swirling microbubble generator that is downsized and simplified so that it can be applied to a small-scale water environment, a substantially spherical vessel having a hollow portion A swirling microbubble generator is proposed in which the gas that is self-sucked from the gas inlet is turned into microbubbles by the swirling flow of the liquid that flows into the gas-liquid outlet, and a swirling gas-liquid mixture containing microbubbles is discharged from the gas-liquid ejection port. It is
前記の通り、液体の旋回流によって気体導入口から気体を自吸して微細気泡化し、微細気泡を含む旋回気液混合液を導出させる旋回式微細気泡発生装置は提案されている。しかしながら、これらの旋回式微細気泡発生装置は、旋回流を生じさせる液体と同じ液体中に導出することにより旋回気液混合液を放出するものであり、旋回流を構成する媒体と異なる媒体中、例えば空気中に導出した場合には、微細気泡を含む旋回気液混合液を導出するのが困難であった。 As described above, there has been proposed a swirl-type microbubble generator in which gas is self-sucked from a gas inlet by a swirl flow of liquid to form microbubbles, and a swirling gas-liquid mixture containing microbubbles is drawn out. However, these swirling micro-bubble generators discharge the swirling gas-liquid mixture into the same liquid as the liquid that creates the swirling flow. For example, when it is drawn into the air, it is difficult to draw out a swirling gas-liquid mixture containing microbubbles.
そこで本発明では、旋回流を構成する媒体と異なる媒体中に放出した場合であっても、旋回している流体中に他の流体を微細にして混合する事のできる流体混合装置を提供することを課題とする。 Therefore, the present invention provides a fluid mixing device that can finely mix other fluids into the swirling fluid even when the fluid is discharged into a medium different from the medium that constitutes the swirling flow. is the subject.
更に本発明では、旋回している液体中に空気等の気体流体を微細にして混入させることのできる流体混合装置(即ち、マイクロバブル発生装置)であって、特に微細気泡を含有する気液混合液を、ミスト状又は液滴状にして空気中に放出する事のできる流体混合装置を提供する。 Further, in the present invention, there is provided a fluid mixing device (that is, a microbubble generating device) capable of finely mixing a gaseous fluid such as air into a swirling liquid, particularly a gas-liquid mixing device containing microbubbles. To provide a fluid mixing device capable of discharging liquid into the air in the form of mist or droplets.
前記課題の少なくとも何れかを解決するべく、本発明では導出口の外側に圧力障壁を設けた流体混合装置を提供する。
即ち本発明では、主流体中に副流体を分散混入させる流体混合装置であって、縦断面形状が円形の内壁面を有する主容器を備えており、当該主容器の内壁面には、その内周面に沿って主流体を案内する主流体導入口が設けられると共に、当該主容器の一方の端部には、当該主容器の軸心方向に副流体を案内する副流体導入口が設けられており、前記主容器における前記副流体導入口が設けられた側とは反対側に存在する他端部には、主容器内で渦流となった主流体を導出する導出口が設けられており、当該導出口の外側には、導出される流体に対する圧力障壁を形成する圧力調整部を設けた流体混合装置を提供する。
In order to solve at least one of the above problems, the present invention provides a fluid mixing device in which a pressure barrier is provided outside the outlet.
That is, in the present invention, a fluid mixing device for dispersing and mixing a secondary fluid in a main fluid is provided with a main container having an inner wall surface having a circular vertical cross-sectional shape, and the inner wall surface of the main container has a A main fluid introduction port is provided for guiding the main fluid along the peripheral surface, and a secondary fluid introduction port is provided at one end of the main container for guiding the secondary fluid in the axial direction of the main container. At the other end of the main container opposite to the side where the secondary fluid inlet is provided, an outlet port is provided for leading out the main fluid that has become a swirling flow within the main container. and a fluid mixing device provided with a pressure regulating portion forming a pressure barrier against the discharged fluid outside the outlet.
前記主流体は水である他、ガソリンなどの液体燃料や、アルコールその他の液体、或いは空気、プロパンガス、又は水素ガス等の気体であって良い。また前記副流体は空気、プロパンガス、又は水素ガス等の気体の他、水、ガソリンなどの液体燃料、又はアルコールその他の液体であって良い。ここで主流体と副流体は相互に異なる状態(液体又は気体)を使用することが望ましく、例えば主流体が水などの液体であれば、副流体は空気等の気体であることが望ましい。また主流体と副流体は相互に異なる限りにおいて、同じ状態(液体又は気体)であっても良く、例えば主流体が空気(気体)であれば、副流体は水素ガス(気体)であって良い。 The main fluid may be water, liquid fuel such as gasoline, liquid such as alcohol, or gas such as air, propane gas, or hydrogen gas. The secondary fluid may be gas such as air, propane gas, or hydrogen gas, liquid fuel such as water or gasoline, or liquid such as alcohol. Here, it is desirable to use different states (liquid or gas) for the main fluid and the secondary fluid. For example, if the primary fluid is liquid such as water, the secondary fluid is preferably gas such as air. In addition, the main fluid and the secondary fluid may be in the same state (liquid or gas) as long as they are different from each other. For example, if the primary fluid is air (gas), the secondary fluid may be hydrogen gas (gas). .
そして主流体が水であって、副流体が空気であれば、当該流体混合装置はマイクロバブル発生装置として利用することができ、主流体がガソリンなどの液体燃料であって、副流体が空気であれば、当該流体混合装置はキャブレターやインジェクターなどとして利用することができる。よって本発明に係る流体混合装置は、主流体と副流体の組み合わせ次第では、各種の工業製品の製造にも使用することができる。 If the main fluid is water and the secondary fluid is air, the fluid mixing device can be used as a microbubble generator, and the main fluid is liquid fuel such as gasoline and the secondary fluid is air. If so, the fluid mixing device can be used as a carburetor, an injector, or the like. Therefore, the fluid mixer according to the present invention can also be used for manufacturing various industrial products depending on the combination of the main fluid and the secondary fluid.
上記本発明の流体混合装置において、前記内壁面は案内された主流体に旋回流を生じさせ、当該旋回流の中心部に生じる負圧空洞部に、前記副流体導入口から副流体を導入し、前記旋回流の圧力が開放される渦崩壊点において、前記副流体が主流体内に混入し、当該渦崩壊点は前記導出口又はその近傍に存在するように構成することが望ましい。また当該渦崩壊点は、導出口から、その開口径の長さ分だけ内側又は外側に存在しても良く、特に散水板を設けた場合には導出口と散水板の間の領域に存在するのが好ましい。 In the fluid mixing device of the present invention, the inner wall surface causes the guided main fluid to generate a swirling flow, and the subfluid is introduced from the subfluid inlet into the negative pressure cavity generated at the center of the swirling flow. Preferably, the secondary fluid is mixed into the main fluid at a vortex breakdown point where the pressure of the swirling flow is released, and the vortex breakdown point is located at or near the outlet. Further, the vortex breakdown point may exist inside or outside of the outlet by the length of the opening diameter. preferable.
前記圧力障壁は、前記渦崩壊点の位置を制御する為に機能することができ、前記導出口における主流体の圧力は、前記圧力調整部に存在する流体の圧力よりも小さいように形成することが望ましい。 The pressure barrier may function to control the location of the vortex breakdown point, wherein the pressure of the main fluid at the outlet is less than the pressure of the fluid present at the pressure regulator. is desirable.
そして上記本発明に係る流体混合装置において、前記主流体は水等の液体であり、前記副流体が空気等の気体である場合には、前記圧力障壁は液溜まりとして形成することができる。その際、前記圧力調整部は当該液溜まりを形成する空間部として具体化することができる。かかる圧力調整部は、前記導出口の周りを包囲する隔壁部と、複数の開口部を備えて前記導出口と対向配置された散水板と、前記隔壁部の径方向外側に設けられた外側空間部とで構成することもできる。かかる外側空間部を設ける事により、副流体が微細状に混入した主流体に対して旋回流を生じさせることができ、当該旋回流において更に副流体の微細化を実現できる。 In the fluid mixing apparatus according to the present invention, when the main fluid is liquid such as water and the secondary fluid is gas such as air, the pressure barrier can be formed as a liquid pool. In this case, the pressure adjustment section can be embodied as a space forming the liquid pool. The pressure adjusting unit includes a partition surrounding the outlet, a sprinkler plate provided with a plurality of openings and arranged opposite to the outlet, and an outer space provided radially outside the partition. It can also be composed of parts. By providing such an outer space portion, a swirl flow can be generated in the main fluid in which the secondary fluid is finely mixed, and the subfluid can be further miniaturized in the swirl flow.
さらに前記圧力障壁としては、副流体が微細状に混入した主流体の放出に抵抗する部材を用いることができ、例えば多孔板やメッシュなどを使用することができる。これらの部材を前記導出口を閉塞するように設けるか、又は導出口から僅かに離間させて配置することによっても渦崩壊点の発生位置を制御することができる。 Furthermore, as the pressure barrier, a member that resists the discharge of the main fluid containing the subfluid in a minute state can be used, such as a perforated plate or a mesh. The vortex breakdown point generation position can also be controlled by providing these members so as to close the outlet or by arranging them at a slight distance from the outlet.
本発明の流体混合装置は、旋回流型の流体混合装置であり、混合された流体導出口の外側には、導出される流体に対する圧力障壁を形成する圧力調整部を設けている。これにより、旋回流における圧力変動による渦崩壊を導出口よりも外側に存在させることができ、旋回流を構成する媒体と異なる媒体中に放出した場合であっても、旋回している流体中に他の流体を微細にして混合する事のできる流体混合装置が実現する。 The fluid mixing device of the present invention is a swirling flow type fluid mixing device, and is provided with a pressure adjusting section that forms a pressure barrier against the discharged fluid outside the mixed fluid outlet port. As a result, vortex breakdown due to pressure fluctuations in the swirling flow can be made to exist outside the outlet, and even if the vortex is discharged into a medium different from the medium that constitutes the swirling flow, A fluid mixing device is realized that can finely mix other fluids.
特に旋回流を構成する主流体が水であり、副流体が空気である場合には、微細気泡を含有するミストまたは液滴を空気中に放出する事のできるマイクロバブル発生装置とすることができる。 In particular, when the main fluid constituting the swirling flow is water and the secondary fluid is air, the microbubble generator can emit mist or droplets containing microbubbles into the air. .
以下、図面を参照しながら、本実施の形態にかかる流体混合装置を具体的に説明する。特に本実施の形態では、主流体として水を使用し、副流体として空気を使用したいわゆるマイクロバブル発生装置10に基づいて具体的に説明する。よって以下では、流体混合装置をマイクロバブル発生装置10として説明する。 Hereinafter, the fluid mixing device according to this embodiment will be specifically described with reference to the drawings. In particular, the present embodiment will be specifically described based on a so-called microbubble generator 10 using water as the main fluid and air as the secondary fluid. Therefore, the fluid mixing device will be described as the microbubble generator 10 below.
図1は第1の実施の形態にかかるマイクロバブル発生装置10を示す(A)A-A矢視断面図、(B)背面図、(C)C-C矢視断面図、(D)正面図であり、図2は当該マイクロバブル発生装置10の分解断面図であり、図3は当該マイクロバブル発生装置10における(A)流体(水および空気)の流れを示すX-X矢視端面図、(B)放水されるマイクロバブル混入水の流れを示す正面図である。 FIG. 1 shows the microbubble generator 10 according to the first embodiment (A) AA cross-sectional view, (B) rear view, (C) CC cross-sectional view, (D) front view 2 is an exploded cross-sectional view of the microbubble generator 10, and FIG. 3 is an XX end view showing the flow of (A) fluid (water and air) in the microbubble generator 10. , (B) is a front view showing the flow of discharged water mixed with microbubbles.
図1に示す様に、この第1の実施の形態にかかるマイクロバブル発生装置10は、水などの主流体や空気などの副流体が案内される主容器11を用いて形成される。かかる主容器11は、中空状であって、その内壁面は球面形状に形成されている。その結果、当該主容器11内には、図1に示す様に先細り形状の円錐体形状の内部空間12が形成される。但し当該内部空間12は、その他にも円柱形状であってもよく、少なくとも軸方向に直交する向きが円形または楕円形状であれば各種形状に形成することができる。当該内部空間12において導入した主流体に旋回流を生じさせるためである。また当該主容器11の内部空間12の後端側、即ち導出口13とは反対側の内面には、半球形状の窪みを、後述する副流体導入口15を囲む様に環状に形成している。 As shown in FIG. 1, the microbubble generator 10 according to the first embodiment is formed using a main container 11 in which a main fluid such as water and a secondary fluid such as air are guided. The main container 11 is hollow and has a spherical inner wall surface. As a result, as shown in FIG. 1, a conical internal space 12 is formed in the main container 11, which is tapered. However, the internal space 12 may also have a cylindrical shape, and can be formed in various shapes as long as the direction orthogonal to the axial direction is circular or elliptical. This is to generate a swirling flow in the main fluid introduced in the internal space 12 . In addition, on the rear end side of the internal space 12 of the main container 11, that is, on the inner surface of the side opposite to the outlet port 13, a hemispherical recess is annularly formed so as to surround the secondary fluid inlet port 15 described later. .
また上記主容器11には、その内周面に沿って主流体を案内する主流体導入口14を設けている。かかる主流体導入口14は、水などの流体を主容器11の内壁面に沿って案内することから、内壁面の接線方向から水を案内するように形成する。本実施の形態において、かかる主流体導入口14は主容器11における長さ方向の略中央に設けているが、導出口13側または後端側に設けることもできる。また当該主容器11の後端側の壁面には、前記内部空間12内に空気等の副流体を取り込むための副流体導入口15を設けている。かかる副流体導入口15は単なる開口として形成することもできるが、図1に示す様に内部空間内に突出するノズル形状に形成するのが望ましい。ノズル状に内部空間12内に突出させることにより、副流体を吸入した後の流れを円滑に行うことができる。
Further, the main container 11 is provided with a main fluid introduction port 14 for guiding the main fluid along its inner peripheral surface. Since the main fluid inlet 14 guides a fluid such as water along the inner wall surface of the main container 11, it is formed so as to guide the water tangentially to the inner wall surface. In the present embodiment, the main fluid inlet 14 is provided substantially in the center of the main container 11 in the longitudinal direction, but it can also be provided on the outlet 13 side or the rear end side. A secondary fluid introduction port 15 for taking in a secondary fluid such as air into the internal space 12 is provided on the rear end side wall surface of the main container 11 . Although the secondary fluid inlet 15 can be formed as a simple opening, it is desirable to form it in the shape of a nozzle protruding into the internal space as shown in FIG. By protruding into the internal space 12 in a nozzle shape, the secondary fluid can flow smoothly after being sucked.
そして上記主容器11の先端側には、内部空間12に導入した水などの主流体を排出する為の導出口13を設けている。かかる導出口13の開口径は、前記主流体導入口14の開口径と同じか、これよりも小さく形成するのが望ましい。 At the tip side of the main container 11, an outlet port 13 for discharging the main fluid such as water introduced into the internal space 12 is provided. It is desirable that the opening diameter of the outlet port 13 is equal to or smaller than the opening diameter of the main fluid inlet port 14 .
以上のように構成した主容器11における導出口13の外側(即ち、下流側)には、主容器11から排出される主流体の流れの抵抗となる圧力障壁16を設けている。かかる圧力障壁16は、本実施の形態では液溜まり16によって実現しており、前記導出口13の外側には、当該液溜まりを形成する為の圧力調整部17を設けている。本実施の形態において当該圧力調整部17は、導出口13の周りを包囲する隔壁部18と、複数の開口部を備えて前記導出口13と対向配置された散水板19と、前記隔壁部18の径方向外側に設けられた外側空間部20とで形成している。 A pressure barrier 16 that resists the flow of the main fluid discharged from the main container 11 is provided outside (that is, on the downstream side) of the outlet port 13 in the main container 11 configured as described above. Such a pressure barrier 16 is realized by a liquid reservoir 16 in the present embodiment, and a pressure adjusting section 17 for forming the liquid reservoir is provided outside the outlet port 13 . In the present embodiment, the pressure adjusting unit 17 includes a partition wall 18 surrounding the outlet 13, a sprinkler plate 19 having a plurality of openings and facing the outlet 13, and the partition 18. It is formed with an outer space portion 20 provided radially outwardly.
かかる隔壁部18の正面側、即ち微細状副流体が分散混合した主流体の放出方向には、複数の開口部を備える散水板19を配置している。前記導出口13と対向状に配置される散水板19は、複数の開口孔を設けたパンチングメタルを用いる他、網部材を使用することができる。この散水板19に形成された開口部の総開口面積は、前記導出口13の開口面積に対して、50%以上、200%以下、特に70%以上、150%以下とすることが望ましい。50%未満であると、微細状副流体が分散混合した主流体を円滑に排出するのが困難となり、200%を超えると圧力障壁16の確保が困難になる為である。かかる散水板19は、図2に示す様に、前記主容器11における導出口13と対向するように配置し、これを内向きフランジ部を有する筒状の保持部材21によって前記主容器11に固定することができる。 A spray plate 19 having a plurality of openings is arranged on the front side of the partition wall 18, that is, in the discharge direction of the main fluid in which the fine secondary fluid is dispersed and mixed. For the sprinkler plate 19 arranged opposite to the outlet 13, a punching metal having a plurality of openings may be used, or a mesh member may be used. The total opening area of the openings formed in the sprinkler plate 19 is desirably 50% or more and 200% or less, particularly 70% or more and 150% or less of the opening area of the outlet port 13 . This is because if it is less than 50%, it becomes difficult to smoothly discharge the main fluid in which the fine sub-fluid is dispersed and mixed, and if it exceeds 200%, it becomes difficult to secure the pressure barrier 16 . As shown in FIG. 2, the sprinkler plate 19 is arranged so as to face the outlet 13 of the main container 11, and is fixed to the main container 11 by a cylindrical holding member 21 having an inward flange. can do.
前記隔壁部18を設ける事により、その径方向外側には外側空間部20が形成される。かかる外側空間部20は、前記導出口13から放出されて、前記散水板19の内側に存在する空間(即ち、液溜まり16)に存在する、微細状副流体が分散混合した主流体を、さらに撹拌する為の空間として機能する。即ち、本実施の形態にかかる流体混合装置では、前記液溜まり16と当該外側空間部20とが一体となって、微細状副流体が分散混合した主流体の撹拌領域として機能することから、微細な副流体同士の結合又は合体の問題を無くすことができる。 By providing the partition wall portion 18, an outer space portion 20 is formed radially outside thereof. The outer space portion 20 discharges the main fluid, which is discharged from the outlet port 13 and exists in the space (that is, the liquid pool 16) inside the sprinkler plate 19, into which the fine sub-fluid is dispersed and mixed. It functions as a space for stirring. That is, in the fluid mixing device according to the present embodiment, the liquid reservoir 16 and the outer space 20 are integrated and function as a stirring region of the main fluid in which the fine secondary fluid is dispersed and mixed. Problems of coupling or coalescence between secondary fluids can be eliminated.
図3は以上のように構成した流体混合装置の動作時における各流体(本実施の形態では、水と空気)の流れを示す(A)X-X矢視端面図、(B)正面図である。この図3に示す様に、前記主流体導入口14から案内された水道水などの主流体は、主容器11の内部空間12内に沿って流れることで螺旋流となる。そして当該内部空間12は導出口13に向かって先細り形状となっており、内壁面に沿って流れる水等の主流体の中心部分には、負圧空洞部が生じる。その結果、前記副流体導入口15から、空気等の副流体が内部空間内(即ち負圧空洞内)に吸引されることになる。そして螺旋流となっている水等の主流体と、負圧空洞部に案内された空気等の副流体は、導出口13に向かって先細り形状になっている領域を通って導出口13を出た領域(即ち、渦崩壊点)において、前記主流体の螺旋流が渦崩壊し、前記空気等の副流体と混合撹拌される。その結果、主流体よりも比重が小さい副流体は微細化し、これが主流体中に分散混入されることになる。即ち、本実施の形態において副流体の微細化(マイクルバブル化)は、前記導出口13よりも下流側で発生している。これは当該導出口13の外側に圧力障壁16が存在する事によるものであり、本実施の形態では、前記導出口13の外側に液溜まりを設けている為である。 FIG. 3 shows the flow of each fluid (in this embodiment, water and air) during operation of the fluid mixing device configured as described above. be. As shown in FIG. 3, the main fluid such as tap water guided from the main fluid inlet 14 flows along the inner space 12 of the main container 11 to form a spiral flow. The internal space 12 is tapered toward the outlet 13, and a negative pressure cavity is generated in the central portion of the main fluid such as water flowing along the inner wall surface. As a result, the secondary fluid such as air is sucked into the internal space (that is, into the negative pressure cavity) from the secondary fluid introduction port 15 . The main fluid, such as water, which forms a spiral flow, and the secondary fluid, such as air, guided to the negative pressure cavity, pass through the area tapered toward the outlet port 13 and exit the outlet port 13. In the region (that is, vortex breakdown point), the helical flow of the main fluid undergoes vortex breakdown and is mixed and agitated with the secondary fluid such as air. As a result, the sub-fluid, which has a lower specific gravity than the main fluid, is finely divided and dispersed and mixed in the main fluid. That is, in the present embodiment, the secondary fluid is made finer (microbubbles) at the downstream side of the outlet port 13 . This is because the pressure barrier 16 exists outside the outlet 13, and this is because the liquid pool is provided outside the outlet 13 in the present embodiment.
当該液溜まり16、即ち導出口13の外側であって前記散水板19の内側に確保された空間内において、前記導出口13から排出された、微細気泡分散含有水は螺旋状に旋回して撹拌され、当該液溜まりと連続する前記外側空間部20内においても撹拌される。これにより前記の圧力障壁(液溜まり16)を確保することにより、微細化した空気等の副流体が再結合する事態を阻止することができる。 In the liquid pool 16, that is, the space secured inside the water sprinkling plate 19 outside the outlet 13, the water containing dispersed microbubbles discharged from the outlet 13 is spirally swirled and stirred. It is also stirred in the outer space 20 that is continuous with the liquid pool. By securing the pressure barrier (liquid pool 16), it is possible to prevent recombination of sub-fluid such as finely divided air.
そして旋回流を生じさせている微細気泡分散含有水は、前記散水板19を通過した後においても旋回流となる。即ち、図3(B)に示す様に、散水板19の各開口孔から放出されるそれぞれが螺旋を描いて放出されることになる。その結果、当該流体混合装置から放出される水はマイクロバブルを含有し、且つ開口孔から放出される夫々が螺旋状であることから、吐出する混合液の分散性を高めた流体混合装置とすることができる。 The fine-bubble-dispersed water, which is causing the swirling flow, becomes the swirling flow even after passing through the sprinkler plate 19 . That is, as shown in FIG. 3(B), the water discharged from each opening of the sprinkler plate 19 forms a spiral. As a result, the water discharged from the fluid mixing device contains microbubbles, and since each of the water discharged from the opening holes has a spiral shape, the fluid mixing device can improve the dispersibility of the mixed liquid to be discharged. be able to.
次に図4~6を参照しながら、他の実施の形態にかかる流体混合装置を具体的に説明する。図4は第2の実施の形態にかかる流体混合装置30を示すC-C矢視端面図であり、特に実施の形態1における前記隔壁部18を省略した流体混合装置としている。即ち、この実施の形態にかかる流体混合装置30では、導出口13から排出されるた主流体と副流体は、散水板19の内側に設けられた圧力障壁(即ち、液溜まり16)によって主流体の渦崩壊が生じ、これによって副流体が微細化されて主流体中に分散混合される。 Next, with reference to FIGS. 4 to 6, a fluid mixing device according to another embodiment will be specifically described. FIG. 4 is a CC arrow end view showing a fluid mixing device 30 according to the second embodiment, and in particular, the fluid mixing device omits the partition portion 18 of the first embodiment. That is, in the fluid mixing device 30 according to this embodiment, the main fluid and the sub-fluid discharged from the outlet port 13 are separated from each other by the pressure barrier (that is, the liquid pool 16) provided inside the spray plate 19. vortex breakdown occurs, whereby the secondary fluid is atomized and dispersed and mixed in the primary fluid.
図5は第3の実施の形態にかかる流体混合装置40を示すC-C矢視端面図であり、この実施の形態では、前記外側空間部20の底面を中心部(隔壁側)が深くなる半球状に形成している。外側空間部20の底面をこのように湾曲させることにより、流体の流れを滞留させることなく円滑にすることができる。 FIG. 5 is a CC arrow end view showing a fluid mixing device 40 according to the third embodiment. It has a hemispherical shape. By curving the bottom surface of the outer space portion 20 in this manner, the flow of fluid can be made smooth without stagnating.
図6は第4の実施の形態にかかる流体混合装置50を示す縦断面図である。この実施の形態にかかる流体混合装置50では、先端側、即ち導出口13側を円錐形状に形成した漏斗状の主容器11を用いており、その内部空間12も先細り形状となっている。そして後端側の壁面には、内壁面の接戦方向に主流体を案内する主流体導入口14を設け、後端側は閉塞部材51で閉塞している。かかる閉塞部材51は、半円形の窪みを環状に設けると共に、その中央部に副流体導入口15を設けて形成されている。また漏斗状に形成した主容器11の導出口13には、これを閉塞する様に散水板19を設けている。当該散水板19は多孔板や網部材によって形成することができ、少なくとも導出口13から放出される主流体に抵抗となる様に形成する。 FIG. 6 is a longitudinal sectional view showing a fluid mixer 50 according to a fourth embodiment. The fluid mixing device 50 according to this embodiment uses a funnel-shaped main container 11 having a conical shape on the tip side, that is, on the outlet port 13 side, and the internal space 12 thereof also has a tapered shape. A wall surface on the rear end side is provided with a main fluid introduction port 14 for guiding the main fluid in the contact direction of the inner wall surface, and the rear end side is closed by a closing member 51 . Such a closing member 51 is formed by providing a semi-circular depression in an annular shape and providing the secondary fluid introduction port 15 in the central portion thereof. In addition, a sprinkling plate 19 is provided so as to close the discharge port 13 of the funnel-shaped main container 11 . The water spray plate 19 can be formed of a perforated plate or a mesh member, and is formed so as to resist at least the main fluid discharged from the outlet 13 .
即ち、この第4の実施の形態にかかる流体混合装置では、前記散水板19が圧力障壁16となっており、当該圧力障壁16の存在により、主流体中に副流体を微細混合させた微細気泡分散含有水を製造することができる。そして液溜まりを設けていない事から、前記渦崩壊点は散水板19内またはその近傍に存在する事になる。 That is, in the fluid mixing apparatus according to the fourth embodiment, the water spray plate 19 serves as a pressure barrier 16, and the presence of the pressure barrier 16 allows microbubbles in which the secondary fluid is finely mixed in the main fluid. Dispersion-containing water can be produced. Since no liquid pool is provided, the vortex breakdown point exists within or near the sprinkler plate 19 .
以上、本実施の形態では主流体を水、副流体を空気としてマイクロバブル分散水を製造する例について説明したが、主流体や副流体はこれらに限ることなく使用することができる。よって、当該流体混合装置は、各種流体の混合装置として、例えばキャブレターやインジェクターなどとしても使用することができる。 As described above, in the present embodiment, an example in which microbubble-dispersed water is produced using water as the main fluid and air as the secondary fluid has been described, but the primary fluid and the secondary fluid are not limited to these. Therefore, the fluid mixing device can be used as a mixing device for various fluids, such as a carburetor or an injector.
本発明にかかる流体混合装置は、マイクロバブル発生装置の他、各種流体を混合させるため、特に副流体を主流体中に分散混合させるために使用することができる。
The fluid mixing device according to the present invention can be used not only as a microbubble generator but also for mixing various fluids, particularly for dispersing and mixing a secondary fluid into a main fluid.
10 マイクロバブル発生装置
11 主容器
12 内部空間
13 即ち導出口
13 導出口
14 主流体導入口
15 副流体導入口
16 圧力障壁(液溜まり)
17 圧力調整部
18 隔壁部
19 散水板
20 外側空間部
21 保持部材
30,40,50 流体混合装置
51 閉塞部材
10 Microbubble generator
11 Main vessel
12 Interior space
13 Outlet
13 Outlet
14 Main fluid inlet
15 Secondary fluid inlet
16 Pressure barrier (liquid pool)
17 Pressure regulator
18 Bulkhead
19 Sprinkler plate
20 Outer space
21 holding member
30,40,50 fluid mixer
51 Closure member
Claims (6)
縦断面形状が円形の内壁面を有する主容器を備えており、
当該主容器の内壁面には、その内周面に沿って主流体を案内する主流体導入口が設けられると共に、当該主容器の一方の端部には、当該主容器の軸心方向に副流体を案内する副流体導入口が設けられており、
前記主容器における前記副流体導入口が設けられた側とは反対側に存在する他端部には、主容器内で渦流となった主流体を導出する導出口が設けられており、
当該導出口の外側には、導出される流体に対する圧力障壁を形成する圧力調整部を設けており、
当該圧力調整部は、前記導出口の周りを包囲する隔壁部と、複数の開口部を備えて前記導出口と対向配置された散水板と、前記隔壁部の径方向外側に設けられた外側空間部とからなることを特徴とする、流体混合装置。
A fluid mixing device for dispersing and mixing a secondary fluid into a main fluid,
A main container having an inner wall surface with a circular vertical cross-sectional shape,
The inner wall surface of the main container is provided with a main fluid inlet for guiding the main fluid along the inner peripheral surface, and a sub-fluid inlet is provided at one end of the main container in the axial direction of the main container. A secondary fluid inlet is provided to guide the fluid,
At the other end of the main container on the side opposite to the side where the secondary fluid inlet is provided, an outlet port is provided for leading out the main fluid that has become a swirling flow in the main container,
A pressure regulating portion is provided outside the outlet port to form a pressure barrier against the fluid to be led out ,
The pressure adjusting unit includes a partition surrounding the outlet, a sprinkler plate having a plurality of openings and arranged opposite to the outlet, and an outer space provided radially outside the partition. A fluid mixing device comprising :
前記旋回流の圧力が開放される渦崩壊点において、前記副流体が主流体内に混入し、
当該渦崩壊点は前記導出口に存在する、請求項1に記載の流体混合装置。
The inner wall surface causes a swirling flow in the guided main fluid, and introduces the secondary fluid from the secondary fluid inlet into a negative pressure cavity generated at the center of the swirling flow,
the secondary fluid mixes into the main body at a vortex breakdown point where the pressure of the swirling flow is released;
2. The fluid mixing device of claim 1, wherein said vortex breakdown point is at said outlet.
前記圧力障壁は液溜まりであって、前記圧力調整部は当該液溜まりを形成する空間部である、請求項1又は2に記載の流体混合装置。
the primary fluid is a liquid and the secondary fluid is a gas;
3. The fluid mixing device according to claim 1, wherein said pressure barrier is a liquid reservoir, and said pressure adjustment section is a space forming said liquid reservoir.
前記旋回流の圧力が開放される渦崩壊点は、前記導出口と散水板の間の領域に存在する、請求項1又は2に記載の流体混合装置。
the outer space portion is connected to a liquid pool secured inside the water spray plate outside the outlet and causes the fluid discharged from the outlet to swirl and agitate;
3. The fluid mixing device according to claim 1 , wherein a vortex breakdown point at which pressure of said swirling flow is released exists in a region between said outlet and a sprinkler plate .
3. The fluid mixing device according to claim 1 , wherein the total opening area of the plurality of openings provided in the sprinkler plate is 50% or more and 200% or less of the opening area of the outlet.
前記散水板に形成された開口部の総開口面積は、前記導出口の開口面積に対して、50%以上、200%以下である、請求項1に記載の流体混合装置。 The outlet opening diameter is equal to or smaller than the opening diameter of the main fluid inlet,
2. The fluid mixing device according to claim 1, wherein the total opening area of the openings formed in the sprinkler plate is 50% or more and 200% or less of the opening area of the outlet.
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PCT/JP2023/045379 WO2024135639A1 (en) | 2022-12-19 | 2023-12-18 | Fluid mixer |
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