JP4725707B2 - Swivel type fine bubble generator and bubble generation method - Google Patents

Description

  The present invention relates to a technical field of a fine bubble generator for efficiently dissolving a gas such as air or oxygen gas in tap water, river water, or other liquids, for example, purifying water quality and reviving a water environment. Belongs.

Most of the conventional aeration, for example, aeration using a microbubble generator installed in an aquatic organism growth device, pressurizes air into the growth water from the pores of a tubular or plate-like microbubble generator installed in the growth tank. The air bubbles are subdivided by blowing them out, or air is put into the growth water flow in which shearing force is formed by rotating blades or bubble jets, etc., and the air is subdivided or pressurized. This is a method of generating bubbles by evaporating air dissolved in water by rapid decompression of water.
In aeration using a fine bubble generator having these functions, basically, necessary adjustments are made according to the amount of air supplied, the number of facilities of each fine bubble generator, etc. It is necessary to dissolve a gas such as water with high efficiency in water and further promote the circulation of water.

Therefore, the present inventor previously has a container body having a cylindrical space whose one end is closed with a wall and the other end is open, a gas introduction hole formed in the wall on the one end, and the cylindrical shape. Developed a micro-bubble generator that consists of a pressurized liquid inlet opening in the tangential direction on a part of the inner wall circumferential surface of the space, purifies the quality of the contaminated water, and revives the contaminated natural water environment Have contributed.
JP 2003-205228 A JP 2003-181259 A JP 2000-000447 A

However, the conventional aeration method using a fine bubble generator is, for example, an air diffusion method using a jet, and no matter how fine pores are provided, bubbles are ejected from the pores in a pressurized state and volume-expanded. Due to the surface tension of the bubbles at that time, as a result, large bubbles having a diameter of several millimeters are generated, and it is difficult to generate bubbles smaller than that, and with the operation for a long time. There were problems of clogging occurring and increasing power costs.
In addition, in a method in which air is put into a water flow in which shear force is formed by rotating blades or bubble jets, etc., and the air is subdivided, a high rotational speed is required to generate cavitation, and the power cost is reduced. There are problems such as blade corrosion and vibration that rapidly progress with the occurrence of problems and cavitation, and there is also a problem that the generation rate of fine bubbles is small.
In addition, in the method in which the gas-liquid two-phase flow collides with other rotating blades and protrusions, for example, in a lake, a fish tank, etc., fish and aquatic small organisms are destroyed, and the environment necessary for the growth of aquatic organisms. This hindered the formation and maintenance of
Further, in the pressurization method, the apparatus is large and expensive, and the operation cost is also large. And by any of the above prior arts, it has been impossible to generate fine bubbles having a diameter of, for example, 20 μm or less on an industrial scale.

Further, in the devices described in Japanese Patent Application Laid-Open No. 2003-205228 (Patent Document 1), Japanese Patent Application Laid-Open No. 2003-181259 (Patent Document 2), and Japanese Patent Application Laid-Open No. 2000-000447 (Patent Document 3), The following problem occurred.
(1) When particulate matter such as fine sand is mixed, the vicinity of the gas introduction part rotates at a high speed of several hundreds of revolutions per second. The problem was that it became difficult and fine bubbles were not generated at all.
(2) The stagnation occurs in the upper liquid part, the rotation speed of the liquid and the introduced gas is reduced, and as a result, the diameter of the fine bubbles cannot be reduced and cannot be generated in large quantities. Had drawbacks.
(3) Since the gas introduction part is installed in a part where the pressure is negative, it is easy to suck (introduce) external gas from here, but this introduction amount is not sufficient in the conventional method. .
That is, there are problems that the gas introduction part is excavated, the device breaks down or breaks, the rotation speed is slow, and the amount of gas introduced is small.

As a result of diligent research, the present inventor has made it possible to generate a large amount of fine bubbles on an industrial scale by extending the life of the apparatus by the invention having the following constitution.
The essential point of the present invention is that a cylindrical space 100 is first provided in an apparatus container as shown in FIG. 1 for explaining the principle of the apparatus of the present invention and for explaining the apparatus of the embodiment. Is closed by a wall body, and the other end side 100B is opened to form a gas introduction hole 80 in the wall body of the one end side 100A. The outlet 101 is formed, a pressurized liquid inlet 500 is opened in a tangential direction on a part of the circumferential surface of the inner wall of the cylindrical space 100, and the wall body on one end side 100A of the cylindrical space 100 is A conical shape or a truncated cone shape 110 ′ protruding toward the other end side 100B is formed, and the space shape of the longitudinal section of the one end side 100A is changed to an M shape, and the swirling gas-liquid outlet 101 on the other end side 100B is formed. Contains fine bubbles The swirling fine bubble generating device is configured to derive the swirling gas-liquid mixture.

Therefore, the apparatus main body or at least the swirling gas / liquid outlet 101 is embedded in the liquid, and the pressurized liquid is pumped into the cylindrical space 100 from the pressurized liquid introducing port 500, so that a swirling flow is generated therein. And a negative pressure portion is formed on the cylindrical tube axis. Due to this negative pressure, the gas is sucked from the gas introduction hole 80, and the gas passes through the tube shaft having the lowest pressure, whereby the thin swirling gas vortex tube portion 60 is formed.
In this cylindrical space 100, a swirling flow is formed from the inlet (pressurized liquid inlet) 500 toward the outlet (swirling gas / liquid outlet) 101, and due to this swirling, the liquid changes from the specific gravity of the liquid to the liquid. The centrifugal force and the centripetal force act on the gas at the same time, so that the liquid part and the gas part can be separated, and the gas continues in a string form to the outlet 101 and is ejected from there. The water) suddenly weakens the turning, and a sudden turning speed difference occurs before and after that. Due to the generation of the swirling speed difference, the filamentous gas vortex tube section 60 is continuously and stably cut. As a result, a large amount of fine bubbles, for example, fine bubbles having a diameter of 10 to 20 μm, are present in the vicinity of the swirling gas-liquid outlet 101. The swirling gas-liquid mixed liquid containing the fine bubbles is discharged into the liquid outside the chamber from the opening on the other end side of the cylindrical space.

  At this time, in the present invention, the wall body on the one end side 100A of the cylindrical space 100 is constituted by the conical shape or the truncated cone shape 110 ′ protruding toward the other end side 100B as described above. Reduce the contact resistance between the surface of the wall or the shape of the truncated cone 110 'and the solid surface, such as sand or dust mixed in the liquid, or the wall surface, and increase the amount of air bubbles in the liquid. It is comprised so that it can be made to.

That is, the configuration of the present invention is as follows.
(1) A container body having a cylindrical space whose one end is closed with a wall and the other end is open, a gas introduction hole formed in the wall on the one end, and an inner wall circumference of the cylindrical space In a fine bubble generating apparatus comprising a pressurized liquid introduction port opened in a tangential direction on a part of a surface, having a conical shape or a truncated cone shape in which a wall body on one end side projects toward the other end side And the cone-shaped or frusto-conical wall body has an inclination angle of 10 ° to 70 °, the space shape of the longitudinal section on one end side is M-shaped, and the cylinder on the other end side A swirling fine bubble generating apparatus characterized in that a swirling gas-liquid mixture containing fine bubbles is led out from an opening of a shaped space.
(2) A container body having a cylindrical space whose one end is closed with a wall and the other end is open, and a pressurized liquid established in a tangential direction on a part of the inner wall circumferential surface of the cylindrical space In the fine bubble generating apparatus comprising an inlet, the one end side wall body is formed of a conical or truncated cone shape projecting toward the other end side, and the conical or truncated cone shape wall body The swirl gas-liquid mixture is configured with an inclination angle of 10 ° to 70 °, the space shape of the longitudinal section on one end side is M-shaped, and contains fine bubbles from the opening of the cylindrical space on the other end side A swirl type fine bubble generator characterized by deriving.

(3) The swirling fine bubble generating device according to (1) or (2), wherein an inclination angle of the conical or frustoconical wall on the one end side is 30 ° to 45 °.
(4) The generation of swirling fine bubbles according to any one of (1) and (3) , wherein the cylindrical space of the container body is an inverted frustoconical space having a cylindrical portion at a lower portion. apparatus.
(5) The swirling fine bubble generator according to any one of (1) and (3) , wherein the cylindrical space of the container body is a frustoconical space.
(6) The swirling fine bubble generating device according to any one of (1) and (3) , wherein the cylindrical space of the container body is a bottle-shaped or wine bottle-shaped space.

(7) The cylindrical space of the container main body is an inverted frustoconical space whose bottom having a cylindrical portion at the bottom is closed, (2) or (3) above, Swirl type fine bubble generator.
(8) The swirling fine bubble generating device according to any one of (2) and (3) , wherein the cylindrical space of the container body is a frustoconical space whose bottom is closed. .
(9) The swivel type according to any one of (2) and (3) , wherein the cylindrical space of the container body is a bottle-shaped or wine bottle-shaped space with a closed bottom surface Fine bubble generator.

(10) A plurality of pressurized liquid inlets opened in a tangential direction in a part of the inner wall circumferential surface of the space are provided at intervals on the inner wall circumference of the same curvature. The swirling fine bubble generating device according to any one of (1) to (9) .
(11) A plurality of pressurized liquid inlets opened in a tangential direction in a part of the inner wall circumferential surface of the space are provided at intervals on the inner wall circumference of different curvatures. The swirling fine bubble generator according to any one of (1) to (10) .
(12) The swivel according to any one of (1) to (11) , wherein the pressurized liquid inlet is formed in a part of the inner wall circumferential surface near the bottom of the space. Type microbubble generator.
(13) The pressurized liquid introduction port is formed in a part of the inner wall circumferential surface in the vicinity of the middle part of the space, described in any one of (1) to (12) above Swivel type micro bubble generator.
(14) The swirling fine bubble generating apparatus according to any one of (1) to (13) , wherein a baffle is disposed immediately before the swirling gas-liquid outlet.

(15) A body having a cylindrical space whose one end is closed by a wall and the other end is open, a gas introduction hole formed in the wall on the one end, and an inner wall circumference of the cylindrical space Consists of a pressurized liquid introduction port opened in the tangential direction in a part of the surface, and is configured with a cone shape or a truncated cone shape projecting the wall body on the one end side toward the other end side, Furthermore, the inclination angle of the conical or frustoconical wall body is 10 ° to 70 °, the space shape of the longitudinal section on the one end side is M-shaped, and the opening of the cylindrical space on the other end side By means of a swirl type fine bubble generator adapted to derive a swirl gas-liquid mixed liquid containing fine bubbles from the section, the liquid near the surface of the conical or frustoconical wall body or solid particles mixed in the liquid and Reduce the contact resistance of the liquid and increase the amount of air bubbles in the liquid. A swirl speed between the first step and the second step of forming a gas vortex tube portion that extends and tapers in the direction of the other end in the cylindrical space and before and after the gas vortex tube portion. A third process of generating a difference and forcibly cutting the gas vortex tube portion to generate fine bubbles and deriving the swirling gas-liquid mixture containing the fine bubbles from the opening on the other end side A swirling fine bubble generating method characterized by the above.
(16) A container main body having a cylindrical space whose one end is closed by a wall and the other end is open, and a pressurized liquid established in a tangential direction on a part of the inner wall circumferential surface of the cylindrical space The wall of the one end side is formed of a conical shape or a truncated cone shape that protrudes toward the other end side, and the inclination angle of the cone-shaped or truncated cone-shaped wall body is set. It is composed of 10 ° to 70 °, the space shape of the longitudinal section on the one end side is M-shaped, and the swirling gas-liquid mixture containing fine bubbles is derived from the opening of the cylindrical space on the other end side. The swirl type microbubble generator characterized in that the contact resistance with the liquid or the solid particles mixed in the liquid in the vicinity of the surface of the conical or frustoconical wall is reduced, and in the liquid A first step of increasing the amount of bubbles mixed into the A second step of forming a gas vortex tube part that extends and tapers in the direction of the other end in the cylindrical space and generates a swirl speed difference between before and after the gas vortex tube part, forcing And a third step of generating a fine bubble by cutting the gas vortex tube portion and deriving a swirling gas-liquid mixed liquid containing the fine bubble from the opening on the other end side. Bubble generation method.

(17) The method for generating swirling fine bubbles according to (15) or (16) above, wherein an inclination angle of the conical or frustoconical wall on the one end side is 30 ° to 45 °.
(18) The swirling microbubble generation according to any one of (15) and (17) , wherein the cylindrical space of the container body is an inverted frustoconical space having a cylindrical portion at a lower portion. Method.
(19) The method of generating swirling fine bubbles according to any one of (15) and (17) above, wherein the cylindrical space of the container body is a frustoconical space.
(20) The method for generating swirling fine bubbles according to any one of (15) and (17) above, wherein the cylindrical space of the container body is a space of a bottle-like shape or a wine bottle shape.

(21) a cylindrical space of the container body, the (16) or (17) Neu Zureka paragraph (1), characterized by the bottom having a cylindrical portion at the bottom is a space of inverted frusto-conical being closed The method of generating swirling fine bubbles as described.
(22) The method for generating swirling fine bubbles according to any one of (16) and (17) , wherein the cylindrical space of the container body is a frustoconical space whose bottom is closed. .
(23) The swivel type according to any one of (16) and (17), wherein the cylindrical space of the container body is a bottle-shaped or wine bottle-shaped space whose bottom is closed. Microbubble generation method.

(24) A plurality of pressurized liquid inlets opened in a tangential direction in a part of the inner wall circumferential surface of the space are provided at intervals on the inner wall circumference of the same curvature. The swirling fine bubble generating method according to any one of (15) to (23) .
(25) A plurality of pressurized liquid inlets opened in a tangential direction in a part of the inner wall circumferential surface of the space are provided at intervals on the inner wall circumference of different curvatures. The swirling fine bubble generating method according to any one of (15) to (24) .
(26) The swivel according to any one of (15) to (25) , wherein the pressurized liquid inlet is formed in a part of the inner wall circumferential surface near the bottom of the space. Type fine bubble generation method.

(27) The pressurized liquid introduction port is formed in a part of an inner wall circumferential surface in the vicinity of the middle part of the space, according to any one of (15) to (26) , A swirling microbubble generation method.
(28) The method of generating swirling fine bubbles according to any one of (15) to (27) , wherein a baffle is disposed immediately before the swirling gas-liquid outlet.

According to the swirling microbubble generator of the present invention, a large amount of microbubbles can be easily generated on an industrial scale, and a highly durable apparatus having a long service life can be provided.
In addition, damage due to grinding or excavation in the vicinity of the gas introduction part can be prevented, the apparatus can be used for a long time, and fine bubbles can be generated even in liquids containing solid particles such as sand. it can.
In addition, the wall body on one end side of the space has a conical shape or a truncated cone shape that protrudes toward the other end side, thereby eliminating the volume of the liquid swirling portion inside the apparatus and further rotating the liquid in the apparatus. By making the part erasable, smaller fine bubbles can be generated by improving the turning speed in the apparatus.
That is, according to the apparatus of the present invention, the turning speed can be increased by 10 to 20% when the same pressure pump is used.
Furthermore, since the introduction of gas is away from the vicinity of the gas introduction port, the swirling speed of the surrounding liquid is further increased, and the gas introduction amount is increased by 10 to 20%. As a result, the generation amount of fine bubbles increases by 20 to 30%.
In the device of the present invention, the wall body on one end side of the space is formed in a conical shape or a truncated cone shape projecting toward the other end side, so that the wall body is inclined, so that the rotation speed is further increased. In other words, it is possible to introduce more gas from the gas introduction portion with the negative pressure, and it is possible to generate a larger amount of finer bubbles. For example, when a normal pump (pressure 0.15 MP, flow rate 20 liters / min) is used, in the case of the device of the present invention, the turning speed is 400 to 500 revolutions per second under the same conditions. In comparison, a large amount of fine bubbles can be generated.

Embodiments of the present invention will be described below with reference to the drawings.
FIG. 1 is a diagram illustrating the principle of an apparatus according to the present invention and an explanatory diagram of an apparatus according to an embodiment. FIG. 2 is an explanatory diagram illustrating an apparatus according to an embodiment of the present invention. 4 is an explanatory view of an embodiment apparatus 4 of the present invention device, FIG. 5 is an explanatory view of the embodiment apparatus 5 of the present invention apparatus, and FIG. 6 is an explanatory view of the embodiment apparatus 6 of the present invention apparatus.
7 is an explanatory view of another embodiment of the apparatus of the present invention, FIG. 8 is an operation explanatory view of the wall on one end side of the container body in the apparatus of the present invention, and FIG. 9 is a container body in the conventional apparatus. FIG. 10 is a detailed explanatory view of a pressurized liquid inlet of the apparatus of the present invention, and FIG. 11 is an explanatory view of another embodiment apparatus of the apparatus of the present invention.
In the figure, 1, 1a to 1f are swirling fine bubble generating devices, 10 is a container, 60 is a swirling gas vortex tube, 80 is a gas introduction hole, 100 is a cylindrical space, 100A is one end side of the cylindrical space, 100B Is the other end side of the cylindrical space, 100a is an inverted frustoconical space having a cylindrical portion at the bottom, 100b and 100c are frustoconical spaces, 100d is a bottle-shaped or wine bottle-shaped space, 100e is a frustoconical space, 100f is an inverted frustoconical space whose bottom surface has a cylindrical part closed, 101 is a swirling gas-liquid outlet, 110 is a conical shape (of a wall), 110 'is a frustoconical shape of (a wall), Reference numeral 500 denotes a pressurized liquid inlet, and θ denotes an inclination angle.

  The swirl type fine bubble generating apparatus of the present invention has one end side 100A closed in the apparatus container 10 and the other end as shown in the principle explanatory view of the apparatus of the present invention in FIG. A cylindrical space 100 having an open side 100B is provided, and a gas introduction hole 80 is formed in the wall of the one end side 100A, and the other end side 100B forms a swirling gas-liquid outlet 101 in the opening. In addition, a pressurized liquid introduction port 500 is opened in a tangential direction on a part of the circumferential surface of the inner wall of the cylindrical space 100, and the wall body on one end side 100A of the cylindrical space 100 is connected to the other end side 100B. It has a conical shape or a truncated cone shape 110 'protruding toward the end, and the space shape of the longitudinal section of the one end side 100A is M-shaped, and includes fine bubbles from the swirling gas-liquid outlet port 101 on the other end side 100B. Swirling gas-liquid mixture Configured to output.

Then, the apparatus 1 main body or at least the swirling gas / liquid outlet 101 is embedded in the liquid, and the pressurized liquid is pumped into the cylindrical space 100 from the pressurized liquid introducing port 500, so that the swirling flow is introduced into the inside. And a negative pressure portion is formed on the cylindrical tube axis. Due to this negative pressure, the gas is sucked from the gas introduction hole 80, and the gas passes through the tube shaft having the lowest pressure, whereby the thin swirling gas vortex tube portion 60 is formed.
In this cylindrical space 100, a swirling flow is formed from the inlet (pressurized liquid inlet) 500 toward the outlet (swirling gas / liquid outlet) 101. With this swirling, the difference in specific gravity between the liquid and the gas is shown in FIG. As shown in (b), centrifugal force acts on the liquid and centripetal force acts on the gas at the same time, so that the liquid part and the gas part can be separated, and the gas continues in a string form to the outlet 101 and is ejected therefrom. At the same time as the ejection, the surrounding hydrolyzed liquid (water) abruptly weakens the turning, and a sudden turning speed difference occurs before and after. Due to the generation of the swirling speed difference, the filamentous gas vortex tube section 60 is continuously and stably cut. As a result, a large amount of fine bubbles, for example, fine bubbles having a diameter of 10 to 20 μm, are present in the vicinity of the swirling gas-liquid outlet 101. And is discharged into the liquid outside the vessel.

In the apparatus 1a of the present invention shown in the explanatory drawing of the apparatus 2 of the embodiment of the apparatus of the present invention shown in FIG. 2, an inverted frustoconical space 100a having a cylindrical portion is first provided in the apparatus container, and an inner wall circle of the space 100a is provided. A pressurized liquid introduction port 500 is opened in a tangential direction in a part of the peripheral surface, and a gas introduction hole 80 is opened in a wall of one end portion 100A of the inverted frustoconical space 100a having the cylindrical portion. The wall body of the side 100A is formed of a conical shape or a truncated cone shape 110 ′ protruding toward the other end side 100B, and an opening is provided on the other end side of the space 100a to provide the swirling gas-liquid outlet 101. Is provided to constitute a microbubble generator.
Therefore, by embedding the main body of the device 1a or at least the swirling gas-liquid outlet 101 in the liquid and pumping the pressurized liquid from the pressurized liquid inlet 500 into the inverted frustoconical space 100a having a cylindrical portion, A swirling flow is generated therein, and a negative pressure portion is formed on the inverted conical tube axis. Due to this negative pressure, the gas is sucked from the gas introduction hole 80, and the gas passes through the tube shaft having the lowest pressure, whereby the thin swirling gas vortex tube portion 60 is formed. In this space 100a, as the cross section of the space 100a is reduced, the swirl flow velocity and the flow velocity toward the outlet increase simultaneously toward the swirl gas-liquid outlet 101. In addition, due to this swirling, due to the difference in specific gravity between the liquid and gas, centrifugal force acts on the liquid and centripetal force acts on the gas at the same time. Then, it is ejected from there. At the same time as the ejection, the turning is suddenly weakened by the surrounding static liquid (for example, water), and a sudden turning speed difference is generated before and after that. Due to the occurrence of this swirl speed difference, the filamentous gas vortex tube section 60 is continuously and stably cut, and as a result, a large amount of fine bubbles, for example, fine bubbles having a diameter of 10 to 20 μm are generated near the outlet 101, It is released into the liquid outside the vessel.

  On the other hand, in the device 1b of the present invention shown in the explanatory diagram of the embodiment device 3 of the device of the present invention shown in FIG. 3, the swirling rising water liquid flow is generated in the inverted frustoconical space 100b and the inner portion thereof. A swirling descending water-liquid flow and a triple swirling flow of a negative pressure swirling cavity at its center are formed. When the gas vortex tube portion 60 that swirls while being tapered is formed and discharged from the outlet 101 through the lower central reflux port 6, the gas vortex tube itself receives the resistance of the discharge passage and generates a difference in swirling speed. It is forcibly cut to generate fine bubbles.

The apparatus 1c of the present invention shown in the explanatory view of the apparatus 4 of the embodiment of the apparatus of the present invention shown in FIG. 4 is an apparatus in which the cylindrical space 100 in the apparatus 1 of the embodiment shown in FIG.
In the swirling fine bubble generating device 1c of the present invention shown in FIG. 4, a conical space 100c is first provided in the device container, and a part of the inner wall circumferential surface of the conical space 100c is pressurized in the tangential direction. A liquid introduction port 500 is opened, a gas introduction hole 80 is opened on one end side 100A of the conical space 100c, and a swirling gas-liquid outlet port 101 is provided on the other end side 100B of the conical space 100c. It constitutes a fine bubble generator.

Therefore, the apparatus main body 1c or at least the swirling gas / liquid outlet port 101 is embedded in the liquid, and the pressurized liquid is pumped into the conical space 100c from the pressurized liquid introducing port 500, whereby a swirling flow is introduced into the conical space 100c. And a negative pressure portion is formed on the conical tube axis.
Due to this negative pressure, the gas is sucked from the gas introduction hole 80, and the gas passes through the tube shaft having the lowest pressure, whereby the thin swirling gas vortex tube portion 60 is formed. In this conical space 100c, a swirling flow is formed from an inlet (pressurized liquid inlet) 500 to an outlet (swirl gas / liquid outlet) 101, and the swirling gas / liquid outlet 101 is expanded in accordance with the cross-sectional enlargement of the conical space 100c. As it goes to, the turning flow velocity and the flow velocity toward the outlet increase simultaneously.
In addition, due to this swirling, due to the difference in specific gravity between the liquid and the gas, centrifugal force acts on the liquid and centripetal force acts on the gas at the same time. It continues to the outlet 101 and is ejected from there, but simultaneously with the ejection, the surrounding static liquid (for example, water) abruptly weakens the turning, and a sudden turning speed difference occurs before and after that. Due to the occurrence of this swirl speed difference, the filamentous gas vortex tube section 60 is continuously and stably cut, and as a result, a large amount of fine bubbles, for example, fine bubbles having a diameter of 10 to 20 μm are generated near the outlet 101, It is released into the liquid outside the vessel.

  Further, the device 1d of the present invention shown in the explanatory diagram of the embodiment device 5 of the device of the present invention shown in FIG. 5 has a cylindrical space 100 in the embodiment device 1 shown in FIG. The device 1e of the present invention shown in the explanatory diagram of the embodiment device 6 of the device of the present invention shown in FIG. 6 is a device composed of a truncated cone-shaped space 100e. Similarly, the container main body is configured with a space in which one end side 100A is closed by a wall body and the other end side 100B is open, and a gas introduction hole 80 is opened in the wall body on one end side 100A. The wall surface of the side 100A is configured to have a conical shape 110 or a truncated cone shape 110 ′ protruding toward the other end side, and the pressurized liquid introduction port 500 extends in a tangential direction to a part of the inner wall circumferential surface of each space. It is an established device Turning fine bubbles in the gas-liquid outlet 101 near occurs and are configured to be released into the vessel out.

  In addition, in the device 1f of the present invention shown in the explanatory view of another embodiment of the device of the present invention shown in FIG. 7, an inverted frustoconical space 100f having a cylindrical portion is first provided in the device container, and an inner wall circle of the space 100f is provided. A pressurized liquid inlet 500 ′ is opened in a part of the peripheral surface in the tangential direction, and the wall body of one end portion 100A of the inverted frustoconical space 100f having the cylindrical portion projects toward the other end side 100B. A fine bubble generator is configured by a conical shape or a truncated cone shape 110 ′, and an opening is provided on the other end side 100B of the space 100f and a swirling gas-liquid outlet 101 is provided.

In the above-described embodiment apparatuses 1 to 6, the description has been made with the apparatus in which the gas introduction hole 80 is formed in the wall body, but the present invention apparatus 1f shown in FIG. For example, a cylindrical space with a closed bottom surface, a truncated cone space with a closed bottom surface, a bottle-shaped or wine bottle-shaped space with a closed bottom surface, etc. The same effect can be obtained even when the gas vortex tube portion 60 is formed by using a gas component dissolved in water by being employed in the apparatus of the present invention.
In addition, pressurized water in which a small amount of gas is added and mixed in water in advance can be continuously introduced from the gas-mixed pressurized liquid inlet 500 ′ in the same manner as in the above embodiment.

  In addition, the device 1 of the present invention is a device in which a baffle 200 is disposed immediately before the swirling gas-liquid outlet 101 of the main body of the container 10 as shown in the explanatory view of the device of another embodiment of the present invention in FIG. You can also.

  That is, as for this invention apparatus shown to Example apparatus 1-6, another Example apparatus, etc., all protrude the wall body of the one end side 100A of each space 100 and 100a-100f toward the other end side 100B. Since the conical shape 110 or the frustoconical shape 110 ′ is used, the surface of the conical shape 110 or the frustoconical shape 110 ′ in the vicinity of the surface of the wall and the solid particles such as sand and dust mixed in the liquid and the wall surface And the amount of bubbles mixed into the liquid can be increased.

Moreover, the pressurized liquid inlet 500 opened in the tangential direction in a part of the inner wall circumferential surface of each space 100, 100a to 100f in the present invention is the details of the pressurized liquid inlet of the apparatus of the present invention in FIG. As shown in the explanatory diagram, a plurality of spaces 100 are provided on the inner wall circumference of the same curvature in the space 100 at intervals (FIG. 10A), or the pressurized liquid inlet 500 has different curvatures in the space 100. A plurality can be provided on the inner wall circumference at intervals (FIG. 10B).
In FIG. 1, the pressurized liquid inlet 500 is formed in a part of the inner wall circumferential surface near the bottom (the other end side 100 </ b> B) of the space, but the inner wall near the middle part of the space. It may be opened on a part of the circumferential surface, or may be opened on a part of the inner wall circumferential surface near one end side 100A of the space.

Normally, the main body of the present invention or at least the swirling gas / liquid outlet 101 is buried in the liquid. In the present invention, the apparatus main body 1 (1a to 1f) may be installed by being buried in a liquid, or may be installed by circumscribing a water tank or the like. In the present invention, water is usually used as the liquid, and air is used as the gas. However, as the liquid, other solvents such as toluene, acetone and alcohol, fuels such as petroleum and gasoline, edible fats and oils, butter and ice cream , Food and beverages such as beer, chemicals such as drinks, health supplies such as bath water, environmental water such as lake water, septic tank contaminated water, etc., and other inert gases such as hydrogen, argon, radon, etc. Further, oxidizing agents such as oxygen and ozone, carbon dioxide, hydrogen chloride, sulfurous acid, acidic gases such as nitrogen oxide and hydrogen sulfide, alkaline gases such as ammonia, and the like can be employed.
In FIG. 1, Pa is the pressure in the swirling liquid part in the conical space, Pb is the pressure in the swirling gas part, Pc is the pressure in the swirling gas part near the gas introduction part, Pd is the pressure in the swirling gas part near the outlet, Pe is the pressure in the outlet swirling liquid part.

The conical shape or frustoconical shape of the wall on the one end side in the device of the present invention has an inclination angle θ of 10 ° to 70 °, preferably 30 ° to 45 °.
The following effects were confirmed for the inclination angle θ.
θ = 0 ° Grinding and excavation if sand is present even for a short time θ = 10 to 20 ° Slight grinding or excavation occurs during long-time operation θ = 30 to 40 ° Optimum angle No grinding even after long-term use θ = 50 ~ 70 ° The tip is too thin and the tip may be damaged by grinding or hydrodynamic force after long-term use.

8 is an operation explanatory diagram of the wall body on one end side of the container main body in the device of the present invention, and FIG. 9 is an operation explanatory diagram of the wall body on one end side of the container main body in the conventional device.
In the apparatus of the present invention, as shown in FIG. 1 and FIG. 2, the pressurized liquid is introduced into the space 100 from the pressurized liquid inlet 500, and the liquid is rotating at an ultrahigh speed in the space 100. When the gas is introduced, the gas rotates around the center of the space 100 to form the gas vortex tube portion 60. At that time, the liquid around the gas vortex tube portion 60 is also rotating. That is, in such a gas-liquid two-phase fluid centrifugal separation and centripetal separation, liquid is collected around and gas is collected at the center. Further, in the vicinity of the gas introduction hole 80, the introduced gas and the rotating liquid collide, and the mixed rotating part 61 of the rotating gas and liquid is formed by mixing the gas and the liquid.
Conventionally, the wall on the one end side of the container 10 body is formed flat, and when the pressurized liquid is introduced from the pressurized liquid introduction port 500 of the device 1 of the present invention and the gas is introduced from the gas introduction hole 80, In the vicinity of the outlet of the gas introduction hole 80 formed in the wall body, that is, immediately after the gas is introduced into the space, the liquid and the gas that rotate at a high speed in the space are mixed, and the gas is introduced in the vicinity of the gas introduction hole 80. The liquid is mixed and rotated to form a mixed rotating portion 61.
For this reason, when the pressurized liquid is a liquid in which solid particles such as sand are mixed, the mixed rotating unit 61 includes a mixture of liquid, gas, and solid particles such as sand, and rotates together. Solid particles such as sand with heavy specific gravity are swept away from the center by centrifugal force, rotate around the inner wall surface of the space, concentrate around the entrance of the gas introduction hole 80, and mix with the gas flow again. It is mixed in the rotating part 61, and after that, it is made to flow outside the central part by centrifugal force and moves to the vicinity of the wall in the space.
As this process is repeated, solid particles such as sand play a role of a grinder at the interface between the liquid and gas, and excavate the vicinity of the outlet of the gas introduction hole 80.
Since the excavation part once made tends to concentrate the flow, a larger excavation part is formed, and the vicinity of the outlet of the gas introduction hole 80 is destroyed, thereby preventing the generation of fine bubbles.

In the device 1 of the present invention, the wall body on one end side 100A of the space 100 is configured with a conical shape 110 or a truncated cone shape 110 ′ protruding toward the other end side 100B, and therefore, a contaminant of solid particles such as sand. Is moved to the vicinity of the wall in the space 100 after being swept to the outside of the central portion by centrifugal force, and moved while rotating on the surface of the truncated cone shape 110 ′. It is mixed in 61 and is made to flow outside the center part again by centrifugal force.
However, when solid particles such as sand move near the wall body of the space 100 and collide with the wall body, they move while rotating on the truncated cone 110 ′, and are formed at the tip of the truncated cone 110 ′. Since the mixed rotating portion 61 is formed in the lower portion not in contact with the gas introduction hole 80, the solid particles such as sand and the vicinity of the outlet of the gas introduction hole 80, that is, the truncated cone of the wall body. There is little contact with the vicinity of the wall surface of the shape 110 ′, and damage to the gas introduction hole 80 and the wall surface can be prevented.
As shown in FIG. 8, a fluid is formed at the lower portion of the tip portion by the rotation generated by the inclined shape of the cone shape or the truncated cone shape at the tip portion of the cone shape 110 or the truncated cone shape 110 ′.
Since the position of the mixed rotating portion 61 is determined by the rotation of the fluid formed by the inclination angle θ of the cone shape 110 or the truncated cone shape 110 ′, the inclination angle θ of the cone shape 110 or the truncated cone shape 110 ′ is Determine in consideration of size and the like.
In addition, as said inclination-angle, it is about 10 degrees-70 degrees, and 30 degrees-40 degrees are especially preferable without the damage of a wall surface.

Further, in the device 1 of the present invention, the wall body on one end side 100A of the space 100 is configured with the conical shape 110 or the truncated cone shape 110 ′ protruding toward the other end side 100B, whereby the wall body is inclined. Therefore, the rotational speed is further increased, and it becomes possible to introduce more gas from the gas introduction section with the negative pressure, and it is possible to generate a larger amount of finer bubbles.
For example, when a normal pump (pressure 0.15 MP, flow rate 20 liters / min) is used, in the conventional wall apparatus, fine bubbles are generated at a rotational speed of 200 revolutions per second or more. Since the turning speed is 400 to 500 revolutions or more per second under the same conditions, a large amount of fine bubbles can be generated as compared with the conventional apparatus.

The constituent material of the device of the present invention may be plastic, metal, glass, polyvinyl chloride, stainless steel, etc., and it is preferable to integrate the constituent parts by bonding or screwing. Since the device of the present invention has high durability and does not break even with a liquid mixed with contaminants such as sand and fine metals, the following fields can be cited as application fields of the fine bubbles generated by the device of the present invention. .
・ Maintain the purification of natural environment by purifying the water quality of dam lakes, lakes, ponds, rivers, seas, etc.
・ Purification in artificial natural waters such as biotopes and breeding of organisms such as fireflies and aquatic plants.
-Industrial use.
・ High-temperature diffusion in steel making, promotion of acid cleaning of stainless steel plates and stainless steel wire Organic matter removal in ultrapure water production plant, removal of organic matter in contaminated water by microbubbles of ozone, increase in dissolved oxygen, sterilization, foaming of synthetic resin Body, for example, urethane foam production, various waste liquid treatment, promotion of mixing ethylene oxide into water in sterilization and sterilization equipment with ethylene oxide, emulsification of defoaming agent, aeration into contaminated water in activated sludge treatment method.
・ Agricultural field Improve the amount of oxygen and dissolved oxygen used for hydroponics and improve the harvest rate.
・ Fisheries Field fish farming, squid aquarium life maintenance, yellowtail culture, artificial generation of seaweed beds, seafood breeding, prevention of red tide.
・ Medical field It is applied to bathtub water to form a fine bubble bath, promote blood flow, and keep bathtub water warm.
・ Reform fuel such as gasoline and light oil.
・ Modification in drinking water such as tap water and water for food production.
・ Washing of lenses and mechanical / electronic parts.

FIG. 2 is a diagram for explaining the principle of the device of the present invention and FIG. Explanatory drawing of the Example apparatus 2 of this invention apparatus Explanatory drawing of Example apparatus 3 of this invention apparatus Explanatory drawing of the Example apparatus 4 of this invention apparatus Explanatory drawing of the Example apparatus 5 of this invention apparatus Explanatory drawing of the Example apparatus 6 of this invention apparatus Explanatory drawing of another embodiment apparatus of the present invention apparatus Action explanatory drawing of the wall body of the one end side of the container body in the device of the present invention Explanatory drawing of the action of the wall on the one end side of the container body in the conventional device Detailed explanatory drawing of the pressurized liquid inlet of the apparatus of the present invention Other embodiment of the apparatus of the present invention

Explanation of symbols

DESCRIPTION OF SYMBOLS 1, 1a-1f Swirling type fine bubble generator 10 Container 60 Swirling gas vortex tube part 80 Gas introduction hole 100 Cylindrical space 100A One end side of cylindrical space 100B The other end side of cylindrical space 100a The reverse which has a cylindrical part in the lower part Frustoconical space 100b, 100c frustoconical space 100d bottle-like or wine bottle-shaped space 100e frustoconical space 100f inverted frustoconical space with a bottom having a cylindrical portion closed 101 swirling gas-liquid outlet 110 Conical shape (wall) 110 'Frustum shape (wall) 500 Pressurized liquid inlet θ Inclination angle

Claims (28)

A container body having a cylindrical space whose one end is closed with a wall and the other end is open, a gas introduction hole formed in the wall on the one end, and a circumferential surface of the inner wall of the cylindrical space In the fine bubble generating device comprising a pressurized liquid inlet port opened in the tangential direction to the part, the one end side wall body is configured in a conical shape or a truncated cone shape protruding toward the other end side. And the inclination angle of the cone-shaped or truncated cone-shaped wall body is 10 ° to 70 °, the space shape of the longitudinal section on the one end side is M-shaped, and the cylindrical space on the other end side is A swirl type microbubble generator characterized in that a swirl gas-liquid mixture containing fine bubbles is led out from an opening. A container main body having a cylindrical space whose one end side is closed by a wall and the other end side is open; a pressurized liquid introduction port which is opened in a tangential direction on a part of an inner wall circumferential surface of the cylindrical space; In the fine bubble generating apparatus, the one-end-side wall body is formed of a cone shape or a truncated cone shape projecting toward the other end side, and the inclination angle of the cone-shaped or truncated cone-shaped wall body Is formed in an angle of 10 ° to 70 °, the space shape of the longitudinal section on one end side is M-shaped, and the swirling gas-liquid mixture containing fine bubbles is derived from the opening of the cylindrical space on the other end side. A swirling fine bubble generator characterized by the above.   3. The swirling fine bubble generating device according to claim 1, wherein an inclination angle of the conical or frustoconical wall on the one end side is 30 ° to 45 °. 4. The swirling fine bubble generating device according to claim 1, wherein the cylindrical space of the container body is an inverted frustoconical space having a cylindrical portion at a lower portion. The swirling fine bubble generator according to any one of claims 1 and 3 , wherein the cylindrical space of the container body is a frustoconical space. The swirling fine bubble generating device according to any one of claims 1 and 3 , wherein the cylindrical space of the container body is a bottle-shaped or wine bottle-shaped space. 4. The swirl type fine bubble generation according to claim 2, wherein the cylindrical space of the container main body is an inverted frustoconical space whose bottom surface having a cylindrical portion is closed. 5. apparatus. Cylindrical space of the container body, pivoting fine bubble generator according to any one of claims 2 or 3, characterized in that a space of frustoconical bottom is closed. The swirling fine bubble generating device according to any one of claims 2 and 3 , wherein the cylindrical space of the container main body is a bottle-shaped or wine bottle-shaped space whose bottom is closed. 2. A plurality of pressurized liquid inlets opened in a tangential direction in a part of the inner wall circumferential surface of the space are provided at intervals on the inner wall circumference of the same curvature. The swirl type fine bubble generator according to any one of? 9 . 2. A plurality of pressurized liquid inlets opened in a tangential direction in a part of the inner wall circumferential surface of the space are provided at intervals on the inner wall circumference of different curvatures. The swirl type fine bubble generator according to any one of to 10 . The swirling microbubble generator according to any one of claims 1 to 11 , wherein the pressurized liquid inlet is formed in a part of the inner wall circumferential surface near the bottom of the space. The swirling fine bubble generating device according to any one of claims 1 to 12 , wherein the pressurized liquid inlet is formed in a part of an inner wall circumferential surface in the vicinity of the middle part of the space. . The swirl type fine bubble generator according to any one of claims 1 to 13 , wherein a baffle is disposed immediately before the swirl gas-liquid outlet. A container body having a cylindrical space whose one end is closed with a wall and the other end is open, a gas introduction hole formed in the wall on the one end, and a circumferential surface of the inner wall of the cylindrical space And a conical or frustoconical shape in which the wall at one end projects toward the other end, and further includes the cone. The inclination angle of the shape or frustoconical wall body is 10 ° to 70 °, the space shape of the longitudinal section on the one end side is M-shaped, and it is fine from the opening of the cylindrical space on the other end side Contact resistance with the liquid or solid particles mixed in the liquid near the surface of the conical or frustoconical wall body by the swirl type fine bubble generator adapted to derive the swirling gas-liquid mixture containing bubbles And increase the amount of bubbles in the liquid A swirl speed between the first step and the second step of forming a gas vortex tube portion that extends and tapers in the direction of the other end in the cylindrical space and before and after the gas vortex tube portion. A third process of generating a difference and forcibly cutting the gas vortex tube portion to generate fine bubbles and deriving the swirling gas-liquid mixture containing the fine bubbles from the opening on the other end side A swirling fine bubble generating method characterized by the above. A container main body having a cylindrical space whose one end side is closed by a wall and the other end side is open; a pressurized liquid introduction port which is opened in a tangential direction on a part of an inner wall circumferential surface of the cylindrical space; And the one end side wall body is formed of a cone shape or a truncated cone shape projecting toward the other end side, and the inclination angle of the cone shape or truncated cone shape wall body is 10 ° to It is configured at 70 °, and the space shape of the longitudinal section on the one end side is M-shaped, and the swirling gas-liquid mixture containing fine bubbles is led out from the opening of the cylindrical space on the other end side. By means of the swirling fine bubble generating device, the contact resistance with the liquid or the solid particles mixed in the liquid near the surface of the conical or frustoconical wall is reduced and mixed into the liquid A first step of increasing the amount of bubbles; The second step of forming a gas vortex tube part that is swirled and led out while extending and tapering in the direction of the other end within the pace, and a difference in swirling speed between the front and rear of the gas vortex tube part, forcing the gas Swirl type microbubble generation characterized by comprising a third step of generating microbubbles by cutting the vortex tube and deriving a swirling gas-liquid mixture containing microbubbles from the opening on the other end side Method. The method of generating swirling fine bubbles according to claim 15 or 16 , wherein an inclination angle of the conical or frustoconical wall on the one end side is 30 ° to 45 °. The method for generating swirling fine bubbles according to any one of claims 15 and 17 , wherein the cylindrical space of the container body is an inverted frustoconical space having a cylindrical portion at a lower portion. The method of generating swirling fine bubbles according to any one of claims 15 and 17 , wherein the cylindrical space of the container body is a frustoconical space. The method for generating swirling fine bubbles according to any one of claims 15 and 17 , wherein the cylindrical space of the container main body is a bottle-shaped or wine bottle-shaped space. 18. The swirl type fine bubble generation according to claim 16 , wherein the cylindrical space of the container body is an inverted frustoconical space whose bottom surface having a cylindrical portion is closed. Method. The method of generating swirling fine bubbles according to any one of claims 16 and 17 , wherein the cylindrical space of the container body is a frustoconical space whose bottom is closed. The method of generating swirling fine bubbles according to any one of claims 16 and 17 , wherein the cylindrical space of the container body is a bottle-shaped or wine bottle-shaped space whose bottom is closed. 16. A plurality of pressurized liquid inlets opened in a tangential direction in a part of the inner wall circumferential surface of the space are provided at intervals on the inner wall circumference of the same curvature. The method of generating swirling fine bubbles according to any one of -23 . 16. A plurality of pressurized liquid inlets opened in a tangential direction in a part of the inner wall circumferential surface of the space are provided at intervals on the inner wall circumference of different curvatures. The method of generating swirling fine bubbles according to any one of -24 . The method of generating swirling fine bubbles according to any one of claims 15 to 25 , wherein the pressurized liquid inlet is formed in a part of the inner wall circumferential surface near the bottom of the space. The method of generating swirling fine bubbles according to any one of claims 15 to 26 , wherein the pressurized liquid introduction port is formed in a part of an inner wall circumferential surface in the vicinity of the middle part of the space. . The method for generating swirling fine bubbles according to any one of claims 15 to 27 , wherein a baffle is disposed immediately before the swirling gas-liquid outlet.

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