WO2004016344A1 - Minute air bubble-containing liquid matter and device for manufacturing the liquid matter - Google Patents

Minute air bubble-containing liquid matter and device for manufacturing the liquid matter Download PDF

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Publication number
WO2004016344A1
WO2004016344A1 PCT/JP2003/001228 JP0301228W WO2004016344A1 WO 2004016344 A1 WO2004016344 A1 WO 2004016344A1 JP 0301228 W JP0301228 W JP 0301228W WO 2004016344 A1 WO2004016344 A1 WO 2004016344A1
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WO
WIPO (PCT)
Prior art keywords
liquid
microbubbles
gas
fixed cylinder
water
Prior art date
Application number
PCT/JP2003/001228
Other languages
French (fr)
Japanese (ja)
Inventor
Takeshi Nakajima
Original Assignee
Aics Co., Ltd.
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Aics Co., Ltd. filed Critical Aics Co., Ltd.
Priority to AU2003207251A priority Critical patent/AU2003207251A1/en
Publication of WO2004016344A1 publication Critical patent/WO2004016344A1/en

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20Mixing gases with liquids
    • B01F23/23Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/233Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements
    • B01F23/2331Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements characterised by the introduction of the gas along the axis of the stirrer or along the stirrer elements
    • B01F23/23315Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements characterised by the introduction of the gas along the axis of the stirrer or along the stirrer elements through a hollow guide surrounding the stirrer element
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20Mixing gases with liquids
    • B01F23/23Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/233Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/05Stirrers
    • B01F27/11Stirrers characterised by the configuration of the stirrers
    • B01F27/111Centrifugal stirrers, i.e. stirrers with radial outlets; Stirrers of the turbine type, e.g. with means to guide the flow
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/27Mixers with stator-rotor systems, e.g. with intermeshing teeth or cylinders or having orifices
    • B01F27/272Mixers with stator-rotor systems, e.g. with intermeshing teeth or cylinders or having orifices with means for moving the materials to be mixed axially between the surfaces of the rotor and the stator, e.g. the stator rotor system formed by conical or cylindrical surfaces
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/80Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
    • B01F27/90Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with paddles or arms 
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/80Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
    • B01F27/90Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with paddles or arms 
    • B01F27/906Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with paddles or arms  with fixed axis
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/80Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
    • B01F27/91Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with propellers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F33/00Other mixers; Mixing plants; Combinations of mixers
    • B01F33/45Magnetic mixers; Mixers with magnetically driven stirrers
    • B01F33/453Magnetic mixers; Mixers with magnetically driven stirrers using supported or suspended stirring elements
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F33/00Other mixers; Mixing plants; Combinations of mixers
    • B01F33/80Mixing plants; Combinations of mixers
    • B01F33/82Combinations of dissimilar mixers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/05Stirrers
    • B01F27/11Stirrers characterised by the configuration of the stirrers
    • B01F27/112Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades
    • B01F27/1121Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades pin-shaped

Definitions

  • the present invention relates to a microbubble-containing liquid material as a useful product or an intermediate product in various technical fields, and an apparatus for producing the same.
  • a substance that releases a small amount of gas into a liquid As the discharge port, a microporous plate, a mesh, a polymer foam having open cells, a sintered body, or the like is used. Since the diameter of the generated bubble is much larger than the diameter of the emission port, it is practically difficult to create a microbubble of ⁇ ⁇ or less.
  • a gas is released into the liquid, and the generated gas-liquid mixture is given a motion such as jetting or swirling to break and refine bubbles by the shear force between the liquid and the liquid, or the gas-liquid mixture.
  • the bubble diameter by this method is usually assumed to be 400 to 500 ⁇ .
  • a rotating cylinder is installed in the fixed cylinder, and gas-liquid mixing
  • There is also a proposal to introduce a compound to make the bubbles finer Japanese Patent Laid-Open No. 5-146667) or a proposal to add a magnetic field effect to this (Japanese Patent Laid-Open No. 11-104646). Neither force is said to be able to consistently produce bubbles with a diameter of 10 m or less.
  • a liquid material containing stable microbubbles having a diameter of 10 ⁇ or less which does not contain impurities such as activators, is used in a gas / liquid or gas / gas reaction process, an organic / inorganic foaming process, and the like.
  • impurities such as activators
  • the present invention solves the above-mentioned problems in the prior art, and an apparatus for easily producing water and other liquids containing stable microbubbles having a diameter of about 10 ⁇ m or less for a long period of time. It is intended to provide various useful microbubble-containing liquids obtained.
  • the gas-liquid mixing device according to claims 13 to 20 (hereinafter referred to as a basic device) or, if necessary, a combined use thereof Use the combination of the additional device and the basic device (claims 21 and 22; hereinafter, this device).
  • the microbubble-containing liquid according to claim 1 is a liquid in which stable bubbles having a diameter of about 10 ⁇ m or less are contained in the liquid, and the production method is not particularly limited. By using this device, it is possible to reliably manufacture.
  • the liquid a single liquid or a mixture of plural liquids can be used depending on the purpose, and one or more kinds of additives can be contained therein.
  • a sol form can be used in addition to a solution.
  • a single gas or a mixture of multiple gases can be used as the gas forming the bubble depending on the purpose, and by controlling the temperature appropriately in the production process, a gas that does not exist as a gas at room temperature can be used. It can be used after evaporation.
  • aerosol forms can also be used. The type of gas and liquid, and the ratio of both, are arbitrarily selected according to the purpose.
  • the liquid containing microbubbles described in claim 2 is a liquid in which the microbubbles of claim 1 are mainly formed by air, and the production method is not particularly limited. Make sure You can do it.
  • the mixing ratio of air and liquid is arbitrarily selected according to the purpose.
  • the liquid containing microbubbles according to claim 3 is a liquid containing water or water containing additives and containing stable air bubbles mainly composed of air having a diameter of about 10 m or less.
  • the mixing ratio of air and water or water containing additives is arbitrarily selected according to the purpose.
  • the microbubble content is more permeable than water in normal conditions. Although the reason for this has not been clarified yet, it is possible to think that the clustering of water is subdivided as a result of the magnetization treatment of water by this device. Also, as the gas-liquid contact area increases with the miniaturization of bubbles, oxygen is sufficiently dissolved in water. The fragmentation of water clusters is also thought to favor oxygen dissolution.
  • the liquid containing microbubbles described in claim 4 is manufactured when the present device or the basic device is used for the purpose of purifying a natural environment or the like.
  • the properties of the liquid material are the same as those described in claim 3.
  • the mixing ratio of air and water is arbitrarily set according to the purpose. For example, a ratio of 4 to 10 water to 1 air is adopted.
  • the gas forming the microbubbles in claim 1 is mainly hydrogen, and the production method is not particularly limited. By using, it is possible to reliably manufacture. In this case, the mixing ratio of liquid and gas-liquid is selected according to the purpose.
  • the liquid containing microbubbles described in claim 6 is the fine bubble-containing liquid described in claim 1.
  • JP2003 / 001228 The gas forming small bubbles is mainly oxygen, and the production method is not particularly limited. For example, by using the present apparatus, the production can be surely performed. In this case, the mixing ratio of liquid and gas-liquid is selected according to the purpose.
  • the liquid containing microbubbles according to claim 7 is a liquid in which the gas forming the microbubbles according to claim 1 is mainly nitrogen.
  • the production method is not particularly limited, but for example, by using the present apparatus, the production can be surely performed. In this case, the mixing ratio of liquid and gas-liquid is selected according to the purpose.
  • the gas that forms the microbubbles described in claim 1 is mainly carbon dioxide.
  • the manufacturing method is not particularly limited, but for example, by using the present apparatus, it is possible to reliably manufacture. In this case, the mixing ratio of liquid and gas-liquid is selected according to the purpose.
  • the gas that forms the microbubbles described in claim 1 is mainly carbon dioxide, and water or water containing an additive is selected as the liquid.
  • the production method is not particularly limited, but for example, by using the present apparatus, the production can be surely performed.
  • the gas-liquid mixing ratio in this case is selected according to the purpose.
  • the gas forming the microbubbles described in claim 1 is mainly ozone.
  • the manufacturing method is not particularly limited, but for example, by using the present apparatus, it is possible to reliably manufacture.
  • the mixing ratio of liquid and gas-liquid is selected according to the purpose.
  • T JP2003 / 001228 The microbubble-containing liquid according to claim 11 is mainly composed of ozone, and water or water containing an additive is selected as the liquid. Things.
  • the production method is not particularly limited, but for example, by using the present apparatus, the production can be surely performed.
  • the gas-liquid mixing ratio in this case is selected according to the purpose.
  • the liquid containing microbubbles according to claim 1 or 2 is a liquid in which the gas forming the microbubbles according to claim 1 is mainly a single type or a plurality of types of alcohol vapors, and fats and oils are selected as the liquid. .
  • the production method is not particularly limited, but for example, by using this apparatus, the production can be surely performed. In this case, the mixing ratio of gas and liquid is selected according to the purpose.
  • FIG. 1 is a sectional view showing an example of a basic device according to the present invention.
  • FIG. 2 is a cross-sectional view showing an example of an arrangement of a stirring rod.
  • FIG. 3 is a sectional view showing an example of a fixed cylinder and a rotary cylinder of the basic device.
  • FIG. 4 is a conceptual diagram showing an example of the combination of the basic device and the additional device in the present invention.
  • a rotating cylinder 25 driven by a motor 23 via a rotating shaft 24 is arranged inside a fixed cylinder 21, and the other end of the rotating shaft is connected to a bearing 26. Supported.
  • a liquid suction port 27 and a suction port 29 are provided at one end of the fixed cylinder 21, and a communication chamber 31 is provided at the other end for communicating the fixed cylinder 21 with the outside. Is done.
  • the communication room is composed of an upper plate 31 a and a lower plate 31 b connected by connecting columns 34.
  • a gas-liquid delivery device 33 driven by a motor 23 is provided in the communication chamber 3 1, and the gas-liquid delivery device 3 3 is operated to send the gas-liquid in the communication chamber 3 1 to the outside, thereby providing communication.
  • the inside of the chamber 31 and the inside of the fixed cylinder 21 become negative pressure, and liquid and gas are introduced into the fixed cylinder 21 from the liquid suction port 27 and the suction port 29, respectively.
  • Various types of gas-liquid delivery devices can be used according to the purpose, for example, a rotary wing.
  • a substantially inverted trapezoidal groove 49 or groove 51 is formed between 45-45 or between the ridges 47-47.
  • the liquid and the gas introduced by the negative pressure pass through the space 52 formed by the inner peripheral surface 41 of the fixed cylinder 21 and the outer peripheral surface 43 of the rotating cylinder 25 to the connecting chamber side. Be guided.
  • the inclination angles a and b of the inclined surfaces 45 'and 47 in the projections 45 and 47 are determined as necessary, but are usually in the range of 20 to 60 degrees.
  • Permanent magnets 35 and 37 are installed on the bottom of grooves 49 and 51.
  • the permanent magnets 35 and 37 can be installed in a combination such as the top surface of the protrusion 45 and the bottom surface of the groove 51 or the bottom surface of the groove 49 and the top surface of the protrusion 47 as necessary.
  • the depth d of the groove in the rotating cylinder 25 is set to be larger than the depth c of the groove in the fixed cylinder 21.
  • the material of the permanent magnets 35 and 37 is selected as necessary, but for example, those containing neodymium or zirconium as a main material are suitable for the purpose of the present invention.
  • a stirrer rotated by a motor 23 is installed, and a check valve 60 is provided accordingly.
  • the stirrer has, for example, a structure in which stirrers 61, 63 are arranged as a pair of upper and lower stirrups on each of opposing surfaces of two disks 65, 67 fixed to the rotating shaft 24, or disks 65, 6
  • the structure is such that any one of the stirring rods in 7 is omitted.
  • a plurality of stirring rods are installed as needed, for example, at positions such as 69 and 71.
  • the whole or a part of the stirrers is preferably provided with a magnetic field generating means and / or an ion generating means, and the magnetic field generating means may be the same as the ion generating means, for example, by installing a permanent magnet.
  • the purpose can be achieved by installing special ceramics or ionic ceramics composed of tourmaline and dielectric ceramics or other appropriate ion generators.
  • the radial width of the cross section of the liquid passage formed between the fixed cylinder 21 and the rotary cylinder 25 is the distance between the tops when the tops of the projections provided on 21 and 25 face each other. It fluctuates regularly as the rotating cylinder rotates, with the narrowest and the widest part between the groove bottoms at that time.
  • the liquid containing bubbles introduced into this passage is spiraled by a combination of a violent movement in the circumferential direction due to the rotation of the rotating cylinder and a slightly slower movement toward the sending means due to the negative pressure provided by the sending means 33. It moves to the communication room 31 side gradually while violently rotating along the trajectory.
  • steps (A) to (D) may individually correspond in principle to the microbubble manufacturing means of the prior art, in the present basic apparatus, these steps are performed by a simple apparatus. Sequentially or simultaneously, the introduced gas-liquid mixture is constantly affected by it during a long, descending spiral. As a result, the bubbles in the liquid containing fine bubbles delivered from the basic device become fine and extremely stable.
  • the manufacturing apparatus described in claim 22 is obtained by adding an additional device to be used together as necessary to the above-described basic device (hereinafter referred to as the present device). For some purposes, only basic equipment may be used. Also, in order to ensure the miniaturization of air bubbles, use a plurality of basic devices connected in series or use a method of recycling the microbubble-containing liquid produced by the basic device back to the basic device. It is also possible.
  • the main additional devices used in combination with the basic device 78 are as follows, in addition to the additive supply device described in claim 21.
  • a gas storage tank 72 required for bubble formation is installed and connected to the basic device intake port 81 via a flow rate control device 80.
  • the required number of storage tanks 72 are installed for each gas, and each is connected to a plurality of basic device intake ports via a flow rate control device 80.
  • Each storage tank, if necessary, or if necessary, via a flow rate control device 80 It is connected to one mixing device 73, and the mixing device and the basic device intake port 81 are connected via a flow rate control device 80.
  • a storage tank for the liquid and a heated vaporizer are installed in place of the gas storage tank 72, and the flow rate control device is installed while taking appropriate temperature holding means. Connected to the basic device inlet or to the mixing device. If necessary, install an air supply pump 79 at an appropriate place in the gas passage.
  • the communication chamber 83 has an airtight structure, and a delivery port 84 is provided at one end of the communication chamber. If it is necessary to store the liquid containing microbubbles, a product storage tank 85 is installed and connected to the outlet.
  • the basic device delivery means is driven by a separately provided motor, and the suction speed of gas and liquid by negative pressure is made independent of the rotation speed of the rotary cylinder.
  • the scale of this equipment can be set in a wide range from small and portable to fixed facilities.
  • the microbubble-containing liquid material in the present invention may be produced by a gas / liquid or gas / gas reaction process, an industrial technology such as an organic / inorganic foaming process, an environment mainly involving oxygen supply, a living technology such as agriculture, aquaculture, food, etc. It can be used in a wide variety of forms, including fire extinguishing and other safety technologies. The various forms are shown below.
  • the produced liquid containing microbubbles is directly led to an external reaction vessel, and a catalyst or heating or the like is performed. It is possible to cause a reaction by adding an action, or to allow a part or all of a gas-liquid reaction to proceed in the present apparatus. If necessary, add a temperature control function to all or part of this device.
  • the gas / gas reaction when each gas that forms an element of the reaction is introduced into the reaction vessel as a gas-liquid mixture, the gas is formed by each reaction element gas that can be produced by a plurality of the present apparatuses.
  • a reaction is caused by the action of a catalyst or heating. Even in this case, by selecting an appropriate liquid, handling can be performed safely and easily even when the reaction element gas has high reactivity.
  • water or an additive may be used as the liquid. When water containing water is selected, it is considered that the new property added to water by the present device has an advantageous effect on the reaction.
  • a gas is introduced in the form of bubbles that forms a sparingly soluble salt by combining with the metal ions that constitute the salt when the salt is dissolved in water, and the salt is precipitated on the solid surface immersed in the solution
  • a liquid containing microbubbles which can be produced by the present apparatus and is mainly composed of stable microbubbles having a diameter of about 10 m or less mainly formed by the gas, is used.
  • the precipitates be formed into a uniform film
  • an artificial pearl is produced by repeatedly depositing a calcium carbonate thin film with an aqueous solution of calcium hydroxide and carbon dioxide
  • the bubbles used are Need to be fine and such
  • the liquid containing microbubbles by the present apparatus is suitable for the purpose.
  • Other special remarks are as described in (K0) above.
  • stable microbubbles having a diameter of about 1 ⁇ or less are mainly air, oxygen, hydrogen, ozone, and rare gases. Or a liquid containing microbubbles formed by one kind of gas or a mixture of two or more kinds of gases.
  • the liquid material has a higher permeability and a smaller bubble diameter than those conventionally used, so that a large detergency can be obtained without using a cleaning agent.
  • the equipment since the equipment is simple, there are few restrictions on the place of use, and continuous supply is easy, it can be applied to a wide range of objects from structures to photomask substrates.
  • a gas-liquid mixture When a gas-liquid mixture is used as the foaming element in the production of the foamed material, use a stable microbubble-containing liquid with a diameter of about 10 ⁇ m or less that can be produced by this device.
  • a. Select the organic substance or inorganic substance before the start of polymerization or hardening as a liquid, and use this device to After polymerization or curing as a substance, b.Select an appropriate liquid substance that is compatible with the organic substance or inorganic substance as the liquid, and mix the liquid substance containing microbubbles with the organic substance or inorganic substance with this device. Either curing the polymerization or resin, or c.
  • the foamed material according to the present invention can contain various kinds of gases or a mixture of plural kinds of gases depending on the purpose in the minute closed cells, and the individual cells are finer than those conventionally used practically.
  • the porosity is easy and accurate depending on the amount of gas introduced during the production of liquid containing microbubbles. It is characterized by being controlled by.
  • (L2) In the production of the polymer foam, the liquid containing microbubbles in which the bubbles described above are mainly formed by nitrogen is used.
  • the foamed material is suitable for use in cases where a fire protection function such as blocking the spread of fire in the duct is required.
  • Other special remarks are as described in (L0) above.
  • (L6) A sol containing silicate or other dispersoid is hardened by sol / gel reaction.
  • the bubbles are mainly formed by air in the liquid containing microbubbles containing stable microbubbles having a diameter of about 10 ⁇ or less, which can be produced by this apparatus.
  • Other special remarks are as described in (L0) above.
  • liquids containing microbubbles containing stable microbubbles with a diameter of about 10 ⁇ or less which can be produced by this device, mainly as a supply source of oxygen or active oxygen, Water or water containing additives, and a liquid containing microbubbles in which microbubbles are mainly formed by air, oxygen, or ozone or a mixture of two or all of them is used.
  • a favorable phenomenon such as a sufficient dissolution of oxygen or ozone, an increase in permeation force, and the like occur, and these are stably produced.
  • the feature is that it is retained.
  • appropriate containers and supply equipment can be used to deal with the situation of the target, and large-scale targets can be supplied directly and continuously from this device.
  • the microbubble-containing liquid described in (M0) above is used for watering a plant.
  • the liquid material permeates the ground more easily than ordinary water, and a sufficient amount of oxygen or active oxygen is stably retained and released gradually, so that the oxygen or activity of the plant can be increased quickly and for a long time.
  • Oxygen can be supplied. This has a remarkable effect on healthy plant growth and disease prevention and recovery.
  • Water used as a liquid contains trace elements and other additives that are beneficial to plants. In addition, it can be more effective. See the previous section for other special notes
  • the basic device is installed by an appropriate means such as a gantry so that the liquid supply port is immersed in water, and the basic device is operated while supplying air from above the water surface to the intake port using a soft vinyl tube or the like.
  • an appropriate means such as a gantry
  • the basic device is operated while supplying air from above the water surface to the intake port using a soft vinyl tube or the like.
  • a water purification function completely different from that of the conventional air blowing is exhibited as described above.
  • appropriate microorganisms and / or chemicals can be introduced as additives into the liquid supply port by a simple auxiliary mechanism to add and improve functions such as decomposition or coagulation of submerged sludge.
  • the basic device or this device can be installed by means such as hanging from a mooring object such as a buoy or raft. It can be kept at an appropriate depth below the water surface and used to control pests such as red tide.
  • a mooring object such as a buoy or raft.
  • Other special notes are as described in (M0) above. For this embodiment, some experiments were conducted to confirm its usefulness. The embodiment will be described below.
  • Example 1 A basic device having a fixed cylinder with a diameter of 200 mm and a length of 700 mm was immersed in a water tank, and the volume ratio of air and water was reduced to about 1 by driving a motor at 1 HP at 1500 rpm. : Introduced at a ratio of 4 and operated for 1 hour while circulating the water in the water tank. Then, the fine bubbles generated in the lower part of the tank were collected and the diameter of the bubbles was measured by laser light scattering. Approximately 40% of those with a diameter of 5 to 10 ⁇ and about 20% of those with a diameter of 2 to 3 m, and it was observed that this state lasted for more than 20 days in a closed container.
  • Example 2 area 1 50 m 2 in the closed pond depth lm, using diameter 15 Omm fixed circular cylinder, length 50 Omm, the basic apparatus one drive motor 0. 5 HP, 15 00 r pm , It was installed in water and operated continuously for 3 weeks in the same manner as in Example 1, and the following results were obtained.
  • Table 1 shows the results of water quality analysis before and after the test.
  • Example 3 The same experiment as in Example 2 was performed for 60 days in a pond with an area of 45 ha and a depth of 3 m. As a result, the head layer at the bottom of the pond with an average thickness of 50 cm before the start was the entire pond. And disappeared. In addition, the hydrogen sulfide concentration near the installation point of the equipment and at a point 70 m from the installation point decreased remarkably 7 days after the start of the test as shown in Table 3.
  • microbubble-containing liquids containing stable microbubbles with a diameter of about 10 m or less that can be produced by this device as fire extinguishing agents or neutralizing / absorbing agents. Since various kinds of gases and liquids forming the liquid material can be used, these can be selected according to the purpose and used as an efficient means. Since it is a liquid containing bubbles, it does not diffuse like a gas and has high spreadability compared to ordinary liquids and stays locally, so fire extinguishing or neutralization / absorption efficiency is high, and Even if this gas is harmful to the human body, the safety is improved compared to the use as a normal gas.
  • the liquid material can be easily used according to the target situation by using an appropriate container and a supply device, and is supplied directly from the device as needed.
  • (N1) As the fire extinguisher, use is made of the liquid containing microbubbles described in (NO) above, in which bubbles are mainly formed by carbon dioxide gas. Since the liquid is water containing microbubbles of carbon dioxide gas, it has a high fire extinguishing function, with a water-blocking effect and a combustion-product temperature-lowering effect in addition to the carbon dioxide gas-blocking effect. Other special remarks are as described in the preceding paragraph (NO). Industrial potential
  • the production method of the present invention it is possible to easily and widely produce a liquid material containing stable microbubbles having a diameter of about 1 Om or less, and as a result, industrial technology, living technology and safety technology can be produced. Many useful or intermediate products are provided in each area.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Mixers With Rotating Receptacles And Mixers With Vibration Mechanisms (AREA)
  • Mixers Of The Rotary Stirring Type (AREA)

Abstract

A device and a method for easily manufacturing liquid matter having stable minute air-bubbles of generally 10 μm or less in diameter provided as products or intermediate products useful for wide ranges of industrial technologies, life technologies, and safe technologies, the device wherein basically the combined treatment of magnetization, pressure fluctuation at high frequencies, shearing, and cavitation is performed for gas-liquid mixture, and gas and liquid forming the liquid matter is properly selected to produce various types of useful products.

Description

明 細 書 微小気泡含有液状物及びその製造装置 技術分野  Description Microbubble-containing liquid and its manufacturing equipment
本発明は諸種の技術分野において有用な製品或いは中間製品とな る微小気泡含有液状物及ぴその製造装置に関するものである。 背景技術  The present invention relates to a microbubble-containing liquid material as a useful product or an intermediate product in various technical fields, and an apparatus for producing the same. Background art
液中に微小気泡を作る技術は従来から多くの提案がなされており、 近年では特に水質改善、 浴槽関連の分野に関心が集まっている。 これら の方法のうち主要なものは、 概ね次のように分類される。  Many proposals have been made for techniques for creating microbubbles in liquids, and in recent years, there has been particular interest in water quality improvement and bathtub-related fields. The main ones of these methods are roughly classified as follows.
( 1 ) 加圧等により液中に気体を過剰に溶解させたものを減圧状態に 導き、 過剰溶解分を気体 (気泡) として析出させるもの。 気泡量は過剰 溶解分以上には出来ない。  (1) A substance in which a gas is dissolved excessively in a liquid by applying pressure, etc., is led to a reduced pressure state, and the excess dissolved component is precipitated as a gas (bubbles). The amount of bubbles cannot exceed the amount of excess dissolved.
( 2 )気体を微量づっ液中に放出するもの。放出口としては微小孔板、 メッシュ、 連続気泡を有する高分子発泡材、 焼結体等が用いられる。 生 成する気泡径は放出口径よりもかなり大きくなるため、 Ι Ο μ πι以下の ような微小気泡を作ることは実用的には困難である。  (2) A substance that releases a small amount of gas into a liquid. As the discharge port, a microporous plate, a mesh, a polymer foam having open cells, a sintered body, or the like is used. Since the diameter of the generated bubble is much larger than the diameter of the emission port, it is practically difficult to create a microbubble of Ι Ιμπι or less.
( 3 ) 液中に気体を放出し、 生成した気液混合物に噴流、 旋回等の運 動を与えて液/液間の剪断力によって気泡を破碎 ·微細化する力 或い は気液混合物と器壁 ·突起等との衝突によつて気泡を破碎 ·微細化する もの。 この方法による気泡径は通常 4 0 0〜5 0 0 μ πιであるとされる。 また、 固定円筒中に回転円筒を設置し、 円筒間の円管壁状細隙に気液混 合物を導入して気泡を微細化する提案 (特開平 5— 1 4 6 6 5 7 ) 或い はこれに磁場作用を付加する提案 (特開平 1 1— 1 0 4 6 1 6 ) もある 力 何れも直径 1 0 m以下の気泡を定常的に製造し得るとはされてい ない。 (3) A gas is released into the liquid, and the generated gas-liquid mixture is given a motion such as jetting or swirling to break and refine bubbles by the shear force between the liquid and the liquid, or the gas-liquid mixture. A device that crushes and miniaturizes bubbles by colliding with vessel walls and projections. The bubble diameter by this method is usually assumed to be 400 to 500 μπι. In addition, a rotating cylinder is installed in the fixed cylinder, and gas-liquid mixing There is also a proposal to introduce a compound to make the bubbles finer (Japanese Patent Laid-Open No. 5-146667) or a proposal to add a magnetic field effect to this (Japanese Patent Laid-Open No. 11-104646). Neither force is said to be able to consistently produce bubbles with a diameter of 10 m or less.
( 4 ) 超音波等の振動を利用するもの。 これには、 振動による液圧で 気泡を開裂 ·微細化させるものと、 液体一固体界面における固体の振動 或いは液体一液体界面における液体間の相対速度差によってによって局 所的に負圧部分をつくり、 ここに生ずる減圧気泡と気体との合体によつ て微小気泡を発生させるものとがあるが、 前者は効率的な問題 (共振を 利用するため、 周波数によって有効な気泡径が限定される) があり、 後 者で得られている気泡径は安定なものとしては 1 0 μ ΐη以下に到達して いない。  (4) Devices that use vibration such as ultrasonic waves. This involves breaking and miniaturizing bubbles with the liquid pressure due to vibration, and creating a negative pressure part locally due to the vibration of the solid at the liquid-solid interface or the relative velocity difference between the liquids at the liquid-liquid interface. However, there are some that generate microbubbles by the coalescence of the decompressed air bubbles and the gas generated here. The former is an efficient problem (the effective bubble diameter is limited by the frequency because of the use of resonance). The bubble diameter obtained in the latter does not reach 10 μΐη or less as a stable one.
( 5 ) 上記の方法の何れか 2つをを組み合わせて使用する場合、 例え ば羽根による攪拌と攪拌に伴レヽ液流中に生ずる負圧部分での減圧気泡の 発生との複合効果においても、 直径 1 0 m以下の気泡の製造に十分な 結果は得られていない。 また、 3者以上の方法を組み合わせた提案は見 出すことが困難である。 更に、 従来の提案においては、 生成した気泡 の安定性については殆ど関心が払われておらず、 実際には界面活性剤を 使用しない限り、 長時間安定な状態を保持できる微小気泡は得られてい ない。 このため、 活性剤等の狭雑物を含まぬ、 直径 1 0 μ πι以下の安定 した微小気泡を含有する液状物は、 気/液或いは気/気反応工程、 有機物 ,無機物の発泡工程等の工業技術、 酸素供給を主体とする環境、 農業、 養殖、 食品等の生活技術或いは泡沫消火等の安全技術など、 広範囲な応 用が期待されるにも拘わらず、 従来実用されていない。 発明の開示 (5) When any two of the above methods are used in combination, for example, in the combined effect of stirring by the blades and generation of depressurized air bubbles in the negative pressure part generated in the recirculating liquid flow accompanying the stirring, Sufficient results have not been obtained for the production of bubbles with a diameter of less than 10 m. It is also difficult to find proposals that combine three or more methods. Furthermore, in the conventional proposals, little attention has been paid to the stability of generated bubbles, and in fact, microbubbles that can maintain a stable state for a long time without using a surfactant have been obtained. Absent. For this reason, a liquid material containing stable microbubbles having a diameter of 10 μππι or less, which does not contain impurities such as activators, is used in a gas / liquid or gas / gas reaction process, an organic / inorganic foaming process, and the like. Despite its widespread application to industrial technology, environment mainly involving oxygen supply, living technology for agriculture, aquaculture, food, etc., and safety technology for foam fire fighting, etc., it has not been practically used. Disclosure of the invention
本発明は、 上記の従来技術における問題点を解決し、 直径略 1 0 μ m以下の安定な微小気泡を長時間保持 ·含有する水その他の液状物を容 易に製造する装置と、 これにより得られる各種の有用な微小気泡含有液 状物とを提供しょうとするものである。  The present invention solves the above-mentioned problems in the prior art, and an apparatus for easily producing water and other liquids containing stable microbubbles having a diameter of about 10 μm or less for a long period of time. It is intended to provide various useful microbubble-containing liquids obtained.
本発明においては、 目的とする微小気泡含有物を得る手段の一つとし て、 請求の範囲 1 3〜 2 0記載の気液混合装置 (以下基本装置と言う) または必要に応じてこれと併用される付加装置と基本装置とを組み合わ せたもの (請求の範囲 2 1, 2 2。 以下、 本装置と言う) を使用する。 請求の範囲 1記載の微小気泡含有液状物は、 液体中に直径略 1 0 μ m以下の安定な気泡を含有させた液状物であって、 製造方法は特に限定 されるものではないが、 例えば本装置を用いることにより、 確実に製造 することが出来る。 上記液体としては目的に応じて単一種液体又は複数 種液体の混合物を使用することが出来、 これらに 1種または複数種の添 加物を含有させることも出来る。 混合物及び添加物含有物の形態として は、 溶液の他、 ゾルの形態のものも使用可能である。 上記気泡を形成す る気体としては目的に応じて単一種気体又は複数種気体の混合物を使用 することが出来、 製造工程に適当な温度制御を施すことにより、 常温で は気体として存在しないものを気化して使用することも出来る。 通常の 気体の他、 エアゾルの形態のものも使用可能である。 気体と液体との種 類及び両者の存在比率は目的に応じて任意に選定される。  In the present invention, as one of means for obtaining the target microbubble-containing material, the gas-liquid mixing device according to claims 13 to 20 (hereinafter referred to as a basic device) or, if necessary, a combined use thereof Use the combination of the additional device and the basic device (claims 21 and 22; hereinafter, this device). The microbubble-containing liquid according to claim 1 is a liquid in which stable bubbles having a diameter of about 10 μm or less are contained in the liquid, and the production method is not particularly limited. By using this device, it is possible to reliably manufacture. As the liquid, a single liquid or a mixture of plural liquids can be used depending on the purpose, and one or more kinds of additives can be contained therein. As a form of the mixture and the additive-containing substance, a sol form can be used in addition to a solution. A single gas or a mixture of multiple gases can be used as the gas forming the bubble depending on the purpose, and by controlling the temperature appropriately in the production process, a gas that does not exist as a gas at room temperature can be used. It can be used after evaporation. In addition to normal gases, aerosol forms can also be used. The type of gas and liquid, and the ratio of both, are arbitrarily selected according to the purpose.
請求の範囲 2記載の微小気泡含有液状物は、 請求の範囲 1 の微小気泡 が主として空気によって形成されたものであって、 製造方法は特に限定 されるものではないが、 例えば本装置を用いることにより、 確実に製造 することが出来る。 空気と液体との混合比率は目的に応じて任意に選定 される。 The liquid containing microbubbles described in claim 2 is a liquid in which the microbubbles of claim 1 are mainly formed by air, and the production method is not particularly limited. Make sure You can do it. The mixing ratio of air and liquid is arbitrarily selected according to the purpose.
請求の範囲 3記載の微小気泡含有液状物は、 水又は添加物を含む水 に直径略 1 0 m以下の空気を主体とする安定な気泡を含有させた液状 物であって、 製造方法は特に限定されるものではないが、 例えば本装置 を用いることにより、 確実に製造することが出来る。 空気と水又は添加 物を含む水との混合比率は目的に応じて任意に選定される。 当該微小気 泡含有物は通常の状態の水よりも浸透力が高い。 この理由は未だ明ら力 にはされていないが、 本装置による水の磁化処理の結果、 水のクラスタ —が細分化されているためとする考えが有力である。 また、 気泡微小化 に伴い気液接触面積が増大する結果、 酸素は十分に水中に溶解する。 水 のクラスターの細分化もまた、 酸素の溶 に有利に働くものと考えられ る。  The liquid containing microbubbles according to claim 3 is a liquid containing water or water containing additives and containing stable air bubbles mainly composed of air having a diameter of about 10 m or less. Although not limited, for example, by using the present apparatus, it is possible to reliably manufacture. The mixing ratio of air and water or water containing additives is arbitrarily selected according to the purpose. The microbubble content is more permeable than water in normal conditions. Although the reason for this has not been clarified yet, it is possible to think that the clustering of water is subdivided as a result of the magnetization treatment of water by this device. Also, as the gas-liquid contact area increases with the miniaturization of bubbles, oxygen is sufficiently dissolved in water. The fragmentation of water clusters is also thought to favor oxygen dissolution.
請求の範囲 4記載の微小気泡含有液状物は、 本装置或いは基本装置 が自然環境浄化等の目的に使用される場合に製造される。 当該液状物の 性質は、 請求の範囲 3記載のものと同様である。 空気と水との混合比 率は、 目的に応じて任意に設定され、 例えば空気 1に対し水 4〜1 0の ような比率が採用される。  The liquid containing microbubbles described in claim 4 is manufactured when the present device or the basic device is used for the purpose of purifying a natural environment or the like. The properties of the liquid material are the same as those described in claim 3. The mixing ratio of air and water is arbitrarily set according to the purpose. For example, a ratio of 4 to 10 water to 1 air is adopted.
請求の範囲 5記載の微小気泡含有液状物は、 請求の範囲 1の微小気 泡を形成する気体が主として水素であるものであり、 製造方法は特に限 定されるものではないが、 例えば本装置を用いることにより、 確実に製 造することが出来る。 この場合の液体及び気液の混合比率は目的に応じ て選定される。  In the liquid containing microbubbles described in claim 5, the gas forming the microbubbles in claim 1 is mainly hydrogen, and the production method is not particularly limited. By using, it is possible to reliably manufacture. In this case, the mixing ratio of liquid and gas-liquid is selected according to the purpose.
請求の範囲 6記載の微小気泡含有液状物は、 請求の範囲 1記載の微 JP2003/001228 小気泡を形成する気体が主として酸素であるものであり、 製造方法は特 に限定されるものではないが、 例えば本装置を用いることにより、 確実 に製造することが出来る。 この場合の液体及び気液の混合比率は目的に 応じて選定される。 The liquid containing microbubbles described in claim 6 is the fine bubble-containing liquid described in claim 1. JP2003 / 001228 The gas forming small bubbles is mainly oxygen, and the production method is not particularly limited. For example, by using the present apparatus, the production can be surely performed. In this case, the mixing ratio of liquid and gas-liquid is selected according to the purpose.
請求の範囲 7記載の微小気泡含有液状物は、 請求の範囲 1の微小気泡 を形成する気体が主として窒素であるものである。 製造方法は特に限定 されるものではないが、 例えば本装置を用いることにより、 確実に製造 することが出来る。 この場合の液体及び気液の混合比率は目的に応じて 選定される。  The liquid containing microbubbles according to claim 7 is a liquid in which the gas forming the microbubbles according to claim 1 is mainly nitrogen. The production method is not particularly limited, but for example, by using the present apparatus, the production can be surely performed. In this case, the mixing ratio of liquid and gas-liquid is selected according to the purpose.
請求の範囲 8記載の微小気泡含有液状物は、 請求の範囲 1記載の微 小気泡を形成する気体が主として炭酸ガスであるものである。 製造方法 は特に限定されるものではないが、 例えば本装置を用いることにより、 確実に製造することが出来る。 この場合の液体及び気液の混合比率は目 的に応じて選定される。  In the liquid containing microbubbles described in claim 8, the gas that forms the microbubbles described in claim 1 is mainly carbon dioxide. The manufacturing method is not particularly limited, but for example, by using the present apparatus, it is possible to reliably manufacture. In this case, the mixing ratio of liquid and gas-liquid is selected according to the purpose.
請求の範囲 9記載の微小気泡含有液状物は、 請求の範囲 1記載の微 小気泡を形成する気体が主として炭酸ガスであり、 液体として水又は添 加物を含む水が選定されたものである。 製造方法は特に限定されるもの ではないが、 例えば本装置を用いることにより、 確実に製造することが 出来る。 この場合の気液の混合比率は目的に応じて選定される。  In the liquid containing microbubbles described in claim 9, the gas that forms the microbubbles described in claim 1 is mainly carbon dioxide, and water or water containing an additive is selected as the liquid. . The production method is not particularly limited, but for example, by using the present apparatus, the production can be surely performed. The gas-liquid mixing ratio in this case is selected according to the purpose.
請求の範囲 1 0記載の微小気泡含有液状物は、 請求の範囲 1記載の 微小気泡を形成する気体が主としてオゾンであるものである。 製造方法 は特に限定されるものではないが、 例えば本装置を用いることにより、 確実に製造することが出来る。 この場合の液体及び気液の混合比率は目 的に応じて選定される。 T JP2003/001228 請求の範囲 1 1記載の微小気泡含有液状物は、 請求の範囲 1記載の 微小気泡を形成する気体が主としてオゾンであり、 液体として水又は添 加物を含む水が選定されたものである。 製造方法は特に限定されるもの ではないが、 例えば本装置を用いることにより、 確実に製造することが 出来る。 この場合の気液の混合比率は目的に応じて選定される。 In the liquid containing microbubbles described in claim 10, the gas forming the microbubbles described in claim 1 is mainly ozone. The manufacturing method is not particularly limited, but for example, by using the present apparatus, it is possible to reliably manufacture. In this case, the mixing ratio of liquid and gas-liquid is selected according to the purpose. T JP2003 / 001228 The microbubble-containing liquid according to claim 11 is mainly composed of ozone, and water or water containing an additive is selected as the liquid. Things. The production method is not particularly limited, but for example, by using the present apparatus, the production can be surely performed. The gas-liquid mixing ratio in this case is selected according to the purpose.
請求の範囲 1 2記載の微小気泡含有液状物は、 請求の範囲 1記載の 微小気泡を形成する気体が主として単一種又は複数種のアルコール蒸気 であり、 液体として油脂類が選定されたものである。 製造方法は特に限 定されるものではないが、 例えば本装置を用いることにより、 確実に製 造することが出来る。 この場合の気液の混合比率は目的に応じて選定さ れる。 図面の簡単な説明  The liquid containing microbubbles according to claim 1 or 2 is a liquid in which the gas forming the microbubbles according to claim 1 is mainly a single type or a plurality of types of alcohol vapors, and fats and oils are selected as the liquid. . The production method is not particularly limited, but for example, by using this apparatus, the production can be surely performed. In this case, the mixing ratio of gas and liquid is selected according to the purpose. BRIEF DESCRIPTION OF THE FIGURES
第 1図 本発明における基本装置の一例を示す断面図である。 FIG. 1 is a sectional view showing an example of a basic device according to the present invention.
第 2図 攪拌棒の配置の一例を示す断面図である。 FIG. 2 is a cross-sectional view showing an example of an arrangement of a stirring rod.
第 3図 基本装置の固定筒と回転筒との一例を示す断面図である。 第 4図 本発明おける基本装置と付加装置との併用の一例を示す概 念図である。 発明を実施するための最良の形態 FIG. 3 is a sectional view showing an example of a fixed cylinder and a rotary cylinder of the basic device. FIG. 4 is a conceptual diagram showing an example of the combination of the basic device and the additional device in the present invention. BEST MODE FOR CARRYING OUT THE INVENTION
最初に、 請求の範囲 1 3〜 2 0に述べた基本装置について、 図面 に従って詳細に説明する。  First, the basic device described in claims 13 to 20 will be described in detail with reference to the drawings.
基本装置 は固定筒 2 1の内部に、 モータ 2 3により回転軸 2 4を介 して駆動される回転筒 2 5を配置し、 回転軸の他端は軸受 2 6によ つて支持される。 固定筒 2 1の一方の端部には吸液口 2 7及び吸気口 2 9が設けられ、 他方の端部には、 固定筒 2 1と外部とを連通するため の連通室 3 1が設置される。 連通室は連結柱 3 4によって連結された 上板 3 1 a及ぴ下板 3 1 bで構成される。 連通室 3 1内にはモータ 2 3により駆動される気液送出装置 3 3を設け、 気液送出装置 3 3が作動 して連通室 3 1内の気液を外部に送出することにより、 連通室 3 1内 及び固定筒 2 1内とが負圧となって、 吸液口 2 7と吸気口 2 9からそれ ぞれ液体と気体とが固定筒 2 1内に導入される。 気液送出装置は目的に 応じて例えば回転翼のような種種の形式のものを用いることが出来る。 固定筒 2 1の内周面 4 1及び回転筒 2 5の外周面 4 3には、 それぞれ 長さ方向にほぼ台形の断面を持つ複数本の堤防状突条が設置され、 この結果、 突条 4 5— 4 5間又は突条 4 7 - 4 7間にはほぼ逆台形状の 溝 4 9または溝 5 1が形成される。 負圧により導入された液体及び気体 は、 このような固定筒 2 1の内周面 4 1と回転筒 2 5の外周面 4 3とに より形成される空間 5 2を通路として連結室側に導かれる。 突起 4 5、 4 7における傾斜面 4 5 '、 4 7, の傾斜角 a、 bは必要に応じて定め られるが、 通常は 2 0〜6 0度の範囲にある。 In the basic device, a rotating cylinder 25 driven by a motor 23 via a rotating shaft 24 is arranged inside a fixed cylinder 21, and the other end of the rotating shaft is connected to a bearing 26. Supported. A liquid suction port 27 and a suction port 29 are provided at one end of the fixed cylinder 21, and a communication chamber 31 is provided at the other end for communicating the fixed cylinder 21 with the outside. Is done. The communication room is composed of an upper plate 31 a and a lower plate 31 b connected by connecting columns 34. A gas-liquid delivery device 33 driven by a motor 23 is provided in the communication chamber 3 1, and the gas-liquid delivery device 3 3 is operated to send the gas-liquid in the communication chamber 3 1 to the outside, thereby providing communication. The inside of the chamber 31 and the inside of the fixed cylinder 21 become negative pressure, and liquid and gas are introduced into the fixed cylinder 21 from the liquid suction port 27 and the suction port 29, respectively. Various types of gas-liquid delivery devices can be used according to the purpose, for example, a rotary wing. On the inner peripheral surface 41 of the fixed cylinder 21 and the outer peripheral surface 43 of the rotating cylinder 25, a plurality of embankment-shaped ridges each having a substantially trapezoidal cross section in the length direction are installed. A substantially inverted trapezoidal groove 49 or groove 51 is formed between 45-45 or between the ridges 47-47. The liquid and the gas introduced by the negative pressure pass through the space 52 formed by the inner peripheral surface 41 of the fixed cylinder 21 and the outer peripheral surface 43 of the rotating cylinder 25 to the connecting chamber side. Be guided. The inclination angles a and b of the inclined surfaces 45 'and 47 in the projections 45 and 47 are determined as necessary, but are usually in the range of 20 to 60 degrees.
溝 4 9及ぴ溝 5 1の底面には永久磁石 3 5、 3 7が設置される。 永久 磁石 3 5、 3 7の設置個所は、 必要に応じ突起 4 5の頂面と溝 5 1の底 面、 或いは溝 4 9の底面と突起 4 7の頂面のような組み合わせが選択さ れる。 いずれの場合においても、 回転筒 2 5における溝の深さ dは、 固 定筒 2 1における溝の深さ cよりも大きく設定される。  Permanent magnets 35 and 37 are installed on the bottom of grooves 49 and 51. The permanent magnets 35 and 37 can be installed in a combination such as the top surface of the protrusion 45 and the bottom surface of the groove 51 or the bottom surface of the groove 49 and the top surface of the protrusion 47 as necessary. . In any case, the depth d of the groove in the rotating cylinder 25 is set to be larger than the depth c of the groove in the fixed cylinder 21.
永久磁石 3 5, 3 7の材質は必要に応じ選定されるが、 例えばネオジ ム又はジルコニウムを主材料とするものは本発明の目的に適している。 固定筒 2 1における吸液口 2 7及ぴ吸気口 2 9の下流側には、 モータ 2 3により回転する攪拌装置を設置しこれに伴って逆止弁 6 0を設け る。 攪拌装置は例えば回転軸 2 4に固定された 2枚の円板 6 5, 6 7の 相対する表面の各々に攪拌棒 6 1 , 6 3を上下一対として配置した構造 又は円板 6 5, 6 7のいずれか一方の攪拌棒を省略した構造とする。 攪 拌棒は必要に応じ複数個設置され、 例えば 6 9, 7 1のような位置に配 置される。 攪拌棒の全個数又は一部の個数には好ましくは磁界発生手段 又はイオン発生手段或いはその双方を備えるものとし、 上記磁界発生手 段としては例えば永久磁石の設置により、 同じく上記イオン発生手段と しては例えばトルマリンと誘電セラミックスとよりなる特殊セラミック スないしイオンセラミックス、 或いは他の適宜なイオン発生装置の設置 により目的を達することが出来る。 The material of the permanent magnets 35 and 37 is selected as necessary, but for example, those containing neodymium or zirconium as a main material are suitable for the purpose of the present invention. On the downstream side of the liquid suction port 27 and the suction port 29 in the fixed cylinder 21, a stirrer rotated by a motor 23 is installed, and a check valve 60 is provided accordingly. The stirrer has, for example, a structure in which stirrers 61, 63 are arranged as a pair of upper and lower stirrups on each of opposing surfaces of two disks 65, 67 fixed to the rotating shaft 24, or disks 65, 6 The structure is such that any one of the stirring rods in 7 is omitted. A plurality of stirring rods are installed as needed, for example, at positions such as 69 and 71. The whole or a part of the stirrers is preferably provided with a magnetic field generating means and / or an ion generating means, and the magnetic field generating means may be the same as the ion generating means, for example, by installing a permanent magnet. For example, the purpose can be achieved by installing special ceramics or ionic ceramics composed of tourmaline and dielectric ceramics or other appropriate ion generators.
基本装置によって安定な微小気泡含有液状物が得られる過程は、 未だ 学術的にも十分に解明されていない部分もあり、 如何なる理論にも拘束 されることを好むものではないが、 例えば微小気泡が主として空気によ つて形成され、 液体が水である場合には概ね次のように考えることが出 来る。  The process of obtaining a stable liquid material containing microbubbles by the basic device is still not well understood scientifically, and it is not preferable to be bound by any theory. It is formed mainly by air, and when the liquid is water, the following can be considered.
(A) 吸液口 2 7および吸気口 2 9からそれぞれ固定筒 2 1内に導 入された水及び空気は、 攪拌装置により混和され、 空気泡を含む液状物 となって固定筒 2 1と回転筒 2 5の間に形成される通路に入る。 攪拌装 置に磁界発生手段が備えられている場合には、 水は磁場を通過するする ことによつて気泡の微細化に有利な新し V、性質を付与される。 水に対す る磁場の影響については、 現象としては認められていても理論的には未 だ解明されない部分が多いが、 導電性物質としての水が磁場を通過する ことによつて起電力が発生し、 水分子が電解若しくはそれに至らぬまで も高レ、エネルギー状態に保持され、 この結果水のクラスターの細分化若 しくはクラスター内部構造の変化が生じ、 水に新しい性質が与えられる とする見解が有力である。 本装置においては回転筒に設置された永久 磁石の回転に伴い磁束が高速移動するため、 通常の水の磁化処理装置の ように水が磁場内を流動する場合に比べて水と磁場との相対速度は遥か に大きく、 起電力の発生に有利である。 また、 攪拌装置にイオン発生手 段が付加されている場合には、 液の導電性の増大により起電力の発生を 大きなものとする。 (A) The water and air introduced into the fixed cylinder 21 from the liquid suction port 27 and the suction port 29, respectively, are mixed by a stirrer to form a liquid material containing air bubbles, and the liquid is mixed with the fixed cylinder 21. It enters the passage formed between the rotary cylinders 25. When the stirring device is provided with a magnetic field generating means, water passes through the magnetic field and is given a new property, V, which is advantageous for miniaturization of bubbles. Although the effect of magnetic fields on water is recognized as a phenomenon, there are many parts that have not been clarified theoretically yet, but water as a conductive substance passes through the magnetic field. As a result, an electromotive force is generated, and the water molecules are maintained at a high level and in an energy state even before the electrolysis or the electrolysis, and as a result, the water cluster is fragmented or the internal structure of the cluster is changed. The view that a new property is given is influential. In this device, the magnetic flux moves at high speed with the rotation of the permanent magnet installed in the rotating cylinder, so that the relative position of water and the magnetic field is smaller than when water flows in a magnetic field as in a normal water magnetizer. The speed is much higher, which is advantageous for generating electromotive force. When an ion generating means is added to the stirrer, the generation of electromotive force is increased by increasing the conductivity of the liquid.
(B) 固定筒 2 1と回転筒 2 5との間に形成された液体通路断面の 半径方向の幅は、 2 1及び 2 5に設けられた突起の頂部が正対した時の 頂部間を最狭、 其の時の溝底部間を最広として、 回転筒の回転に伴って 規則的に変動する。 この通路に導入された気泡を含む液体は、 回転筒の 回転による円周方向の激しい運動と、 送出手段 3 3の齎す負圧による送 出手段側へのやや緩徐な運動との合成により、 スパイラル状の軌跡に沿 つて激しく回転しつつ徐々に連通室 3 1側へ移動する。 その間、 気泡を 含む液体には通路の幅の変動に伴う速度変化によりベルヌィの定理に従 う内部圧力の急激な変動が高い周波数で生起し、 これによつて気泡の著 しい細分化を生ずる。 また、 回転筒の回転数が十分に大きく、 圧力変動 の周波数が閾値を超える場合には、 液体中の負圧部分にキヤビティが生 じ、 これによつて微小気泡の発生が促進される。  (B) The radial width of the cross section of the liquid passage formed between the fixed cylinder 21 and the rotary cylinder 25 is the distance between the tops when the tops of the projections provided on 21 and 25 face each other. It fluctuates regularly as the rotating cylinder rotates, with the narrowest and the widest part between the groove bottoms at that time. The liquid containing bubbles introduced into this passage is spiraled by a combination of a violent movement in the circumferential direction due to the rotation of the rotating cylinder and a slightly slower movement toward the sending means due to the negative pressure provided by the sending means 33. It moves to the communication room 31 side gradually while violently rotating along the trajectory. Meanwhile, in the liquid containing bubbles, abrupt changes in the internal pressure according to Bernoulli's theorem occur at a high frequency due to the change in velocity due to the change in the width of the passage, thereby causing significant fragmentation of the bubbles. If the rotation speed of the rotary cylinder is sufficiently high and the frequency of the pressure fluctuation exceeds the threshold value, cavities are generated in the negative pressure portion in the liquid, thereby promoting the generation of microbubbles.
(C) また、 気泡を含む液体は、 上記通路を移動する間、 絶えず固 定筒及ぴ回転筒に設けられた突起との衝突によつて受ける剪断或いは固 定筒及ぴ回転筒に設けられた溝の深さが固定筒側がより深いために起き る内外液間の速度差による剪断の作用を受け、 これによつても気泡の細 分化を生ずる。 (C) Further, the liquid containing air bubbles is continuously provided in the fixed cylinder and the rotating cylinder due to the collision with the projection provided on the fixed cylinder and the rotating cylinder while moving in the above passage. Due to the deeper groove on the fixed cylinder side Shearing is caused by the velocity difference between the inner and outer fluids, which also causes fragmentation of air bubbles.
(D) 更に、 回転筒の回転に伴う液体圧力の高周波変動は、 固定筒 壁の高調波での共振を惹起し、 壁 ·液界面に生ずるキヤビテーションに よって気泡はさらに微細化する。  (D) Further, the high-frequency fluctuation of the liquid pressure accompanying the rotation of the rotating cylinder causes resonance of the fixed cylinder wall at higher harmonics, and the bubbles are further miniaturized by cavitation generated at the wall-liquid interface.
上記 (A) 乃至 (D) の過程は個々には従来技術における微小気泡製 造手段と原理的に一致するものもあるが、 本基本装置にあってはこれら の過程が簡易な装置によつて逐次又は同時に生起し、 導入された気液混 合物はスパイラルを描きつつ降下する長い行程中、 絶えずそれらの作用 を受ける。 これにより、 基本装置より送出された微細気泡含有液状物中 の気泡は微細かつ極めて安定なものとなる。  Although the above steps (A) to (D) may individually correspond in principle to the microbubble manufacturing means of the prior art, in the present basic apparatus, these steps are performed by a simple apparatus. Sequentially or simultaneously, the introduced gas-liquid mixture is constantly affected by it during a long, descending spiral. As a result, the bubbles in the liquid containing fine bubbles delivered from the basic device become fine and extremely stable.
請求の範囲 2 2記載の製造装置は、 上述の基本装置に、 必要に応じ て併用される付加装置を加えたもの (以下本装置と言う) である。 目 的によっては、 基本装置のみが使用される場合もある。 また、 気泡の微 細化を確実にするため、 基本装置を複数台直列に連結して使用するか、 基本装置によつて製造された微小気泡含有液体を再度基本装置にリサイ クルする方法を取ることも可能である。  The manufacturing apparatus described in claim 22 is obtained by adding an additional device to be used together as necessary to the above-described basic device (hereinafter referred to as the present device). For some purposes, only basic equipment may be used. Also, in order to ensure the miniaturization of air bubbles, use a plurality of basic devices connected in series or use a method of recycling the microbubble-containing liquid produced by the basic device back to the basic device. It is also possible.
本装置において、基本装置 7 8と併用される付加装置の主要なものは、 請求の範囲 2 1記載の添加物供給装置の他、 通常以下の如くである。  In the present device, the main additional devices used in combination with the basic device 78 are as follows, in addition to the additive supply device described in claim 21.
( a ) 気泡形成に必要な気体の貯蔵槽 7 2を設置し、 流速制御装 置 8 0を介して基本装置吸気口 8 1に接続する。 複数の混合気体によつ て気泡を形成する場合には、各気体ごとに必要数の貯蔵槽 7 2を設置し、 各々流速制御装置 8 0を介して複数設けられた基本装置吸気口に接続す る力 若しくは必要があれば各貯蔵槽を各々流速制御装置 8 0を介して 一個の混合装置 7 3に結合し、 更に混合装置と基本装置吸気口 8 1とを 流速制御装置 8 0を介して接続する。 常温で液体のものの蒸気を気泡形 成に使用する場合には、 気体貯蔵槽 7 2に代えて当該液体の貯蔵槽及び 加熱気化装置を設置し、 適当な温度保持手段を講じつつ流速制御装置を 介して基本装置吸気口又は混合装置に接続する。 必要に応じ気体の送行 路の適当個所に送気ポンプ 7 9を設置する。 (a) A gas storage tank 72 required for bubble formation is installed and connected to the basic device intake port 81 via a flow rate control device 80. When bubbles are formed by a plurality of gas mixtures, the required number of storage tanks 72 are installed for each gas, and each is connected to a plurality of basic device intake ports via a flow rate control device 80. Each storage tank, if necessary, or if necessary, via a flow rate control device 80 It is connected to one mixing device 73, and the mixing device and the basic device intake port 81 are connected via a flow rate control device 80. When vapor of liquid at normal temperature is used for bubble formation, a storage tank for the liquid and a heated vaporizer are installed in place of the gas storage tank 72, and the flow rate control device is installed while taking appropriate temperature holding means. Connected to the basic device inlet or to the mixing device. If necessary, install an air supply pump 79 at an appropriate place in the gas passage.
( b ) 必要な液体の貯蔵槽 7 5を設置し、 流速制御装置 7 7を介 して基本装置吸液口 8 2に接続する。 複数の液体を混合して使用する場 合には、 各液体ごとに必要数の貯蔵槽 7 5を設置し、 各々流速制御装置 7 7を介して複数設けられた基本装置吸液口に接続する力、 若しくは必 要があれば各貯蔵槽 7 5を各々流速制御装置 7 7を介して一個の混合装 置 7 4に結合し、 更に混合装置と基本装置吸液口 8 2とを流速制御装置 7 7を介して接続する。 必要に応じ液体の送行路の適当個所に送液ボン プ 7 6を設置する。  (b) Install a necessary liquid storage tank 75 and connect it to the basic device suction port 82 via the flow rate control device 77. When using a mixture of multiple liquids, install the required number of storage tanks 75 for each liquid, and connect them to a plurality of basic device suction ports via flow rate control devices 77 If necessary, each storage tank 75 is connected to one mixing device 74 via a flow control device 77, and the mixing device and the basic device suction port 82 are further connected to a flow control device. 7 Connect via 7. Install a liquid feed pump 76 at an appropriate place in the liquid feed path as needed.
( c ) 連通室 8 3を気密構造とし、 連通室の一端に送出口 8 4を 設ける。 微小気泡含有液状物を貯蔵する必要がある場合は製品貯蔵槽 8 5を設置し、 送出口と連結する。  (c) The communication chamber 83 has an airtight structure, and a delivery port 84 is provided at one end of the communication chamber. If it is necessary to store the liquid containing microbubbles, a product storage tank 85 is installed and connected to the outlet.
( d ) 必要に応じ基本装置回転筒の回転速度を可変とする。  (d) The rotation speed of the rotating cylinder of the basic device is made variable as necessary.
( e ) 必要に応じ基本装置送出手段の駆動を別途設備されたモー タで行い、 負圧による気 ·液の吸引速度を回転筒の回転速度から独立し たものとする。  (e) If necessary, the basic device delivery means is driven by a separately provided motor, and the suction speed of gas and liquid by negative pressure is made independent of the rotation speed of the rotary cylinder.
( f ) 必要に応じ基本装置固定筒溝底面および回転筒溝底面の一方 又は双方に発振板を設置し、 キヤビテーシヨン発生効果を向上させる。 永久磁石の材質及ぴ形状を適宜に選定することにより発振板の機能を付 加してもよい。 (f) If necessary, install an oscillator plate on one or both of the bottom of the fixed device groove and the bottom of the rotating tube groove to improve the cavitation generation effect. By appropriately selecting the material and shape of the permanent magnet, the function of the oscillation plate can be added. May be added.
( g ) 必要に応じ本装置の全体又は一部に断熱処理を含む温度制 御 ·保持機構を付加する。  (g) If necessary, add a temperature control / holding mechanism including heat insulation treatment to the whole or part of this device.
本装置の規模は小型可搬式のものから固定施設まで、 広範囲に設定す ることが出来る。  The scale of this equipment can be set in a wide range from small and portable to fixed facilities.
次に、 上述の装置を使用して 製造することが出来る微小気泡含有 液状物の実施形態について説明する。  Next, an embodiment of a microbubble-containing liquid that can be produced using the above-described apparatus will be described.
本発明における微小気泡含有液状物は、 気/液又は気/気反応工程、 有機物 ·無機物の発泡工程等の工業技術、 酸素供給を主体とする環境、 農業、 養殖、 食品等の生活技術或いは泡沫消火等の安全技術など、 広範 囲にわたり種種の形態での実用が可能である。 以下にその各種の形態を 示す。  The microbubble-containing liquid material in the present invention may be produced by a gas / liquid or gas / gas reaction process, an industrial technology such as an organic / inorganic foaming process, an environment mainly involving oxygen supply, a living technology such as agriculture, aquaculture, food, etc. It can be used in a wide variety of forms, including fire extinguishing and other safety technologies. The various forms are shown below.
工業技術における実施の形態  Embodiment in Industrial Technology
(K0) 気/液反応において、 反応要素気体が気液混合物として反応の 場に供給される場合、 気泡が主として当該気液反応の反応要素である気 体によって形成される、 本装置により製造し得る微小気泡含有液状物を 使用する。 該液状物は適当な貯蔵容器から供給することも、 本装置から 直接供給することも出来る。 該液状物中の気泡は従来実用的に得られて いるものよりも微小化されており、 気液接触面積が大きいため反応の進 行に有利である。 微小気泡含有液状物の一方の構成要素である液体は必 要に応じて選定され、 適宜な選定により当該気体が高い反応性を有する 場合にも取り扱いを安全 ·容易に行うことが出来る。 場合によっては当 該気液反応の反応要素である液体を使用することにより、 製造された当 該微小気泡含有液状物を直接外部反応容器に導き、 触媒或いは加熱等の 作用を加えて反応を起こさせること、 或いは本装置内で気液反応の一部 或いは全部を進行させることも可能である。 必要に応じ、 本装置の全体 又は一部に温度制御機能を付加する。 また、 気/気反応においては、 当 該反応の要素を形成する各気体を気液混合物として反応容器へ導入する 場合において、 複数の本装置により製造し得る、 各反応要素気体によつ て形成された微小気泡を含む複数の微小気泡含有液状物を使用し、 触媒 或いは加熱等の作用により反応を生起させる。 この場合においても、 適 宜な液体の選定により、 該反応要素気体が高い反応性を有する場合にも 取り扱いを安全 '容易に行うことが出来る。 また、 これら気/液或いは 気/気反応において、 本装置により製造し得る、 直径略 1 Ο μ ΐη以下の 安定な微小気泡を含む微小気泡含有液状物を使用する際、 液体として水 又は添加物を含む水が選定された場合には、 本装置によって水に付加さ れた新しい性質が反応に有利に作用することが考えられる。 (K0) In a gas / liquid reaction, when the reaction element gas is supplied to the reaction site as a gas-liquid mixture, bubbles are mainly formed by the gas that is the reaction element of the gas-liquid reaction. Use the resulting liquid containing microbubbles. The liquid can be supplied from a suitable storage container or directly from the apparatus. Bubbles in the liquid material are smaller than those conventionally obtained practically, and have a large gas-liquid contact area, which is advantageous for the progress of the reaction. The liquid which is one of the constituents of the liquid containing microbubbles is selected as necessary, and handling can be performed safely and easily by appropriate selection even when the gas has high reactivity. In some cases, by using a liquid that is a reaction element of the gas-liquid reaction, the produced liquid containing microbubbles is directly led to an external reaction vessel, and a catalyst or heating or the like is performed. It is possible to cause a reaction by adding an action, or to allow a part or all of a gas-liquid reaction to proceed in the present apparatus. If necessary, add a temperature control function to all or part of this device. In the gas / gas reaction, when each gas that forms an element of the reaction is introduced into the reaction vessel as a gas-liquid mixture, the gas is formed by each reaction element gas that can be produced by a plurality of the present apparatuses. Using a plurality of microbubble-containing liquids containing microbubbles, a reaction is caused by the action of a catalyst or heating. Even in this case, by selecting an appropriate liquid, handling can be performed safely and easily even when the reaction element gas has high reactivity. In addition, in such gas / liquid or gas / gas reaction, when a liquid containing microbubbles containing stable microbubbles having a diameter of about 1 μμΟη or less that can be produced by this apparatus is used, water or an additive may be used as the liquid. When water containing water is selected, it is considered that the new property added to water by the present device has an advantageous effect on the reaction.
(K1) 水素添加、 接触水素添加、 水素化分解等水素を反応要素の一 つとする気液反応において、 本装置により製造し得る、 直径が略 1 Ο μ m以下の安定な微小気泡が主として水素によつて形成される微小気泡含 有液状物を反応の水素源として使用する。その他の特記事項は上記 (K0) に述べたところと同様である。  (K1) In gas-liquid reactions using hydrogen as one of the reaction elements, such as hydrogenation, catalytic hydrogenation, and hydrocracking, stable microbubbles with a diameter of approximately 1 μm or less that can be produced by this device are mainly hydrogen. The liquid containing microbubbles formed by the reaction is used as a hydrogen source for the reaction. Other remarks are the same as described in (K0) above.
(K2) 酸化等酸素を反応要素の一つとする気液反応において、 本装 置により製造し得る、 直径が略 1 0 μ ΐη以下の安定な微小気泡が主とし て酸素によつて形成される微小気泡含有液状物を反応の酸素源として使 用する。 その他の特記事項は上記 (Κ0) に述べたところと同様である。  (K2) In a gas-liquid reaction using oxygen as one of the reaction elements such as oxidation, stable microbubbles with a diameter of about 10 μ μη or less that can be produced by this device are mainly formed by oxygen. The liquid containing microbubbles is used as the oxygen source for the reaction. The other special notes are the same as those described in (Κ0) above.
(Κ3) 炭酸ガスを反応要素の一つとする気液反応において、 本装置 により製造し得る、 直径略 1 0 m以下の安定な微小気泡が主として炭 酸ガスによって形成される微小気泡含有液状物を反応の炭酸ガス源とし て使用する。 その他の特記事項は上記 (K0) に述べたところと同様で ある。 (Κ3) In a gas-liquid reaction using carbon dioxide as one of the reaction elements, stable microbubbles with a diameter of about 10 m or less that can be produced The liquid containing microbubbles formed by the acid gas is used as a carbon dioxide gas source for the reaction. Other remarks are the same as those described in (K0) above.
(K4) ェステル交換反応等気相のアルコールを反応要素の一つとす る気液反応において、 本装置により製造し得る、 直径略 1 0 / ΐη以下の 安定な微小気泡が主としてアルコール蒸気によつて形成される微小気泡 含有液状物を反応のアルコール源として使用する。 その他の特記事項は 上記 (K0) に述べたところと同様である。  (K4) In a gas-liquid reaction such as a ester exchange reaction in which a gas-phase alcohol is one of the reaction elements, stable microbubbles having a diameter of about 10 / ΐη or less that can be produced by this device are mainly generated by alcohol vapor. The microbubble-containing liquid formed is used as a source of alcohol for the reaction. Other special notes are the same as those described in (K0) above.
(K5) PCB及びダイォキシン (以下 DXN と言う) 類の分解に、 本 装置により製造し得る、 直径略 1 0 μ ΐη以下の安定な微小気泡が主とし て空気またはオゾンによって形成され、 液体が水又は添加物を含む水で ある微小気泡含有液状物を使用する。 PC 或いは DXNを含む処理対象 に該微小気泡含有液状物を加えて攪拌する力、、 又は本装置に水、 空気及 び該処理対象を同時に導入し、 該微小気泡含有液状物を製造しつつ処理 対象と接触させることによって、 PCB或いは DXNを分解することが出 来る。 必要に応じ、 酸化チタンその他の触媒を捕足的に使用することに より、更に効果を確実なものとすることが可能である。場合によっては、 処理対象を含む液と空気とを直接本装置に導入し、 処理を行うことも出 来る。 その他の特記事項は上記 (K0) 記載の通りである。  (K5) For the decomposition of PCBs and dioxins (hereinafter referred to as DXN), stable microbubbles with a diameter of about 10 μΐη or less, which can be produced by this device, are mainly formed by air or ozone, and the liquid is water. Alternatively, use a liquid containing microbubbles, which is water containing additives. Force to add the liquid containing microbubbles to the processing target containing PC or DXN and agitate, or introduce water, air and the processing target into this device at the same time, and process while producing the liquid containing microbubbles. By contacting the object, the PCB or DXN can be decomposed. If necessary, the effect can be further ensured by using titanium oxide and other catalysts as a supplement. In some cases, the liquid containing the object to be treated and the air may be directly introduced into the device to perform the treatment. Other special remarks are as described in (K0) above.
(K6) 気体燃料の液体中燃焼装置において、 燃料ガスと空気または 酸素との混合物を気泡の形で加熱対象液体中に供給する場合、 本装置に より製造し得る、 直径略 1 0 μ ιη以下の安定な微小気泡が主として燃料 ガスと空気または酸素との混合物によって形成される微小気泡含有液状 物を使用する。 該液状物は安定で且つ浮上'放散を起こさないため、 効 率の良い着火、燃焼を行うことが出来る。 その他の特記事項は上記 (K0) 記載の通りである。 (K6) When a mixture of fuel gas and air or oxygen is supplied to the liquid to be heated in the form of bubbles in a gaseous fuel-in-liquid combustion device, the diameter can be manufactured with this device, approximately 10 μιη or less. A liquid containing microbubbles in which stable microbubbles are mainly formed by a mixture of fuel gas and air or oxygen is used. The liquid material is stable and does not emit Highly efficient ignition and combustion can be performed. Other special remarks are as described in (K0) above.
(K7) 過酸化水素の製造に際し、 水素及ぴ酸素を気泡として水中に 導入して反応を起こさせる方法を用いる場合において、 本装置により製 造し得る、 直径略 1 0 μ πι以下の安定な微小気泡が主として酸素によつ て形成される微小気泡含有液状物及び微小気泡が主として水素によって 形成される微小気泡含有液状物を使用する。 該液状物中の気泡は従来使 用されているものに比べて微小であるため反応の進行に有利であり、 安 定であるため安全且つ容易に取り扱うことが出来る。 その他の特記事項 は上記 (Κ0)記載の通りである。  (K7) When hydrogen peroxide and oxygen are introduced as bubbles into water to produce a reaction in the production of hydrogen peroxide, a stable product with a diameter of about 10 μππι or less that can be produced by this device is used. A liquid material containing microbubbles in which microbubbles are mainly formed by oxygen and a liquid material containing microbubbles in which microbubbles are mainly formed by hydrogen are used. The bubbles in the liquid material are finer than those conventionally used, which is advantageous for the progress of the reaction, and are stable and can be handled safely and easily. Other special remarks are as described in () 0) above.
(Κ8) 船舶の走行抵抗減少のため船底と水との間に気泡層を形成す る場合に、 本装置により製造し得る、 直径略 1 0 μ m以下の安定な微小 気泡が主として空気によつて形成される微小気泡含有液状物を使用す る。 該液状物は安定で且つ浮上 ·放散を起こさないため、 安定な気泡層 を形成することが出来る。 その他の特記事項は上記 (K0)記載の通りで める。  (Κ8) When a bubble layer is formed between the bottom of the ship and water to reduce the running resistance of the ship, stable microbubbles with a diameter of about 10 μm or less that can be produced by this device are mainly composed of air. Use the liquid containing microbubbles that is formed as a result. Since the liquid material is stable and does not float or diffuse, a stable bubble layer can be formed. Other special notes are as described in (K0) above.
(K9) 塩類の水溶液中に、 水溶すると当該塩を構成する金属イオン と結合して難溶性の塩を生ずる気体を気泡の形で導入し、 溶液中に浸漬 された固体表面に当該塩を析出させる場合において、 本装置により製造 し得る、 直径略 1 0 m以下の安定な微小気泡が主として当該気体によ つて形成される微小気泡含有液状物を使用する。 析出物が均一な膜状に なることを求められる場合、 例えば水酸ィ匕カルシウム水溶液と炭酸ガス によつて炭酸カルシゥム薄膜を繰り返し析出させて人工真珠を製造する 場合には、 使用される気泡が微細であることが必要とされ、 そのような 目的に対しては本装置による微小気泡含有液状物が適している。 その他 の特記事項は上記 (K0) 記載の通りである。 (K9) In a salt solution, a gas is introduced in the form of bubbles that forms a sparingly soluble salt by combining with the metal ions that constitute the salt when the salt is dissolved in water, and the salt is precipitated on the solid surface immersed in the solution In this case, a liquid containing microbubbles, which can be produced by the present apparatus and is mainly composed of stable microbubbles having a diameter of about 10 m or less mainly formed by the gas, is used. When it is required that the precipitates be formed into a uniform film, for example, when an artificial pearl is produced by repeatedly depositing a calcium carbonate thin film with an aqueous solution of calcium hydroxide and carbon dioxide, the bubbles used are Need to be fine and such The liquid containing microbubbles by the present apparatus is suitable for the purpose. Other special remarks are as described in (K0) above.
(K10)気泡を含む水を洗浄に使用する場合において、 本装置により 製造し得る、 直径略 1 Ο μ πι以下の安定な微小気泡が主として空気、 酸 素、 水素、 オゾン及び希ガスのうち何れか 1種類の気体若しくは 2種類 以上の気体混合物によって形成される微小気泡含有液状物を使用する。 該液状物は従来使用されているものに比べて浸透性が高く、 気泡径が小 さいため洗浄剤を用いることなく大きな洗浄力が得られる。 また、 装置 が簡易で使用場所の制約が少なく、 連続供給も容易であるため、 構造物 からフォトマスク基板に至る広範な対象に適用が可能である。  (K10) When water containing bubbles is used for washing, stable microbubbles having a diameter of about 1 μμπι or less, which can be produced by this device, are mainly air, oxygen, hydrogen, ozone, and rare gases. Or a liquid containing microbubbles formed by one kind of gas or a mixture of two or more kinds of gases. The liquid material has a higher permeability and a smaller bubble diameter than those conventionally used, so that a large detergency can be obtained without using a cleaning agent. In addition, since the equipment is simple, there are few restrictions on the place of use, and continuous supply is easy, it can be applied to a wide range of objects from structures to photomask substrates.
(L0) 発泡材の製造において、 発泡要素として気液混合物が使用さ れる場合、 本装置により製造し得る、 直径略 1 0 μ m以下の安定な微小 気泡含有液状物を使用する。 この目的に対しては、 骨格となる有機物ま たは無機物の性質に応'じて、 a .液体として重合或いは硬ィヒ開始前の当該 有機物または無機物を選定し、 本装置により微小気泡含有液状物として 後重合或いは硬化させるか、 b .液体として当該有機物または無機物と親 和性のある適当な液状物を選定し、 本装置により微小気泡含有液状物と したものを当該有機物または無機物と混和後重合或レヽは硬化させるか、 c .液体としてゾル状の当該有機物または無機物を選定し、 本装置により 微小気泡含有液状物として後ゾル /ゲル反応を利用して硬化させるかの 何れかの方法が使用される。 本発明にかかる発泡材は微小独立気泡中に 目的に応じ種種の気体又は複数種の混合気体を含有させることが出来、 且つ個々の気泡が従来実用的に使用されているものよりも微小であり、 空隙率が微小気泡含有液状物製造時の気体導入量によつて容易且つ正確 に制御されることを特色とする。 (L0) When a gas-liquid mixture is used as the foaming element in the production of the foamed material, use a stable microbubble-containing liquid with a diameter of about 10 μm or less that can be produced by this device. For this purpose, depending on the nature of the organic or inorganic substance serving as the skeleton, a. Select the organic substance or inorganic substance before the start of polymerization or hardening as a liquid, and use this device to After polymerization or curing as a substance, b.Select an appropriate liquid substance that is compatible with the organic substance or inorganic substance as the liquid, and mix the liquid substance containing microbubbles with the organic substance or inorganic substance with this device. Either curing the polymerization or resin, or c. Selecting the organic or inorganic substance in the form of a sol as the liquid and curing it using the post-sol / gel reaction as a liquid containing microbubbles with this device used. The foamed material according to the present invention can contain various kinds of gases or a mixture of plural kinds of gases depending on the purpose in the minute closed cells, and the individual cells are finer than those conventionally used practically. The porosity is easy and accurate depending on the amount of gas introduced during the production of liquid containing microbubbles. It is characterized by being controlled by.
(L1) 高分子発泡材の製造において、 本装置により製造し得る、 直 径略 1 0 μ m以下の安定な微小気泡を含む微小気泡含有液状物におい て、 気泡が主として空気によって形成される微小気泡含有液状物を使用 する。 その他の特記事項は前項 (L0) 記載の通りである。  (L1) In the production of a polymer foam material, in a microbubble-containing liquid material containing stable microbubbles having a diameter of about 10 μm or less, which can be produced by this device, micro bubbles in which bubbles are mainly formed by air Use a liquid containing bubbles. Other special remarks are as described in the previous section (L0).
(L2) 高分子発泡材の製造において、 前項の気泡が主として窒素に よって形成される微小気泡含有液状物を使用する。 当該発泡材はダク ト内の延焼遮断等防火機能を必要とする場合の使用に適する。 その他の 特記事項は上記 (L0) 記載の通りである。  (L2) In the production of the polymer foam, the liquid containing microbubbles in which the bubbles described above are mainly formed by nitrogen is used. The foamed material is suitable for use in cases where a fire protection function such as blocking the spread of fire in the duct is required. Other special remarks are as described in (L0) above.
(L3) 高分子発泡材の製造において、 前項の気泡が主として炭酸ガ スによつて形成された微小気泡含有液状物を使用する。 当該発泡材は ダクト内の延焼遮断等防火機能を必要とする場合の使用に適する。 その 他の特記事項は上記 (L0) 記載の通りである。  (L3) In the production of a polymer foam material, a liquid containing microbubbles in which the bubbles described in the preceding paragraph are mainly formed by carbon dioxide is used. The foamed material is suitable for use when a fire prevention function such as blocking fire in a duct is required. Other special remarks are as described in (L0) above.
(L4) 高分子発泡材の製造において、 前項の気泡が主として窒素と 炭酸ガスとの適宜の割合の混合気体によって形成される微小気泡含有液 状物を使用する。 当該発泡材は垂直ダクト内等での延焼に際し、 下方か らの延焼には窒素が、 上方からの延焼には炭酸ガスがそれぞれ未燃焼部 をカバーして延焼を防止する機能を有する。 その他の特記事項は上記 (L0) 記載の通りである。  (L4) In the production of a polymer foam, a liquid containing microbubbles in which the bubbles described in the preceding paragraph are mainly formed by a mixed gas of nitrogen and carbon dioxide at an appropriate ratio is used. When the foam is spread in a vertical duct or the like, nitrogen spreads from below, and carbon dioxide gas spreads from above. Other remarks are as described in (L0) above.
(L5) 発泡コンクリートの製造に際し、 本装置により製造し得る、 直柽略 1 0 m以下の安定な微小気泡を含む微小気泡含有液状物におい て、 気泡が主として空気によって形成される微小気泡含有液状物を使用 する。 その他の特記事項は上記 (L0) 記載の通りである。  (L5) In the production of foamed concrete, a liquid containing microbubbles containing stable microbubbles of approximately 10 m or less, which can be produced by this device, is a liquid containing microbubbles whose bubbles are mainly formed by air. Use something. Other special remarks are as described in (L0) above.
(L6) 珪酸塩その他を分散質とするゾルをゾル /ゲル反応によって硬 化させて透明な無機質材料を製造する場合に際し、 本装置により製造し 得る、 直径略 1 0 μ πι以下の安定な微小気泡を含 む微小気泡含有液状 物において、 気泡が主として空気によって形成される微小気泡含有液状 物を使用する。 気泡が微小なため透明性を損なうことが少なく、軽量で 断熱性 ·耐熱性に優れた透明材を得ることが出来る。 その他の特記事項 は上記 (L0) 記載の通りである。 (L6) A sol containing silicate or other dispersoid is hardened by sol / gel reaction. In the case of producing a transparent inorganic material by converting into a liquid, the bubbles are mainly formed by air in the liquid containing microbubbles containing stable microbubbles having a diameter of about 10 μπι or less, which can be produced by this apparatus. Use a liquid containing microbubbles. Since the bubbles are very small, transparency is not impaired, and a transparent material that is lightweight and has excellent heat insulation and heat resistance can be obtained. Other special remarks are as described in (L0) above.
生活技術における実施の形態  Embodiment in Life Technology
(M0) 生活関連の諸分野において、 主として酸素或いは活性酸素供 給源として、 本装置により製造し得る、 直径略 1 0 μ πι以下の安定な微 小気泡を含む微小気泡含有液状物において、 液体が水又は添加物を含む 水であり、 微小気泡が主として空気又は酸素又はオゾン或いはこれらの 中の 2者若しくは全者の混合物によって形成される微小気泡含有液状物 を使用する。 既述の如く、 当該液状物では本装置によって水に新しい性 質が付与される結果、 酸素又はオゾンの十分な溶存、 浸透力の増加等目 的に有利な現象を生じ、 且つこれらが安定に保持されることが特色であ る。 実施に当たっては、 適当な容器と供給機器によって対象の状況に応 じた対処が可能であり、 大規模な対象に対しては本装置からの直接 ·連 続的な供給を行うことも出来る。  (M0) In various fields related to daily life, liquids containing microbubbles containing stable microbubbles with a diameter of about 10 μππι or less, which can be produced by this device, mainly as a supply source of oxygen or active oxygen, Water or water containing additives, and a liquid containing microbubbles in which microbubbles are mainly formed by air, oxygen, or ozone or a mixture of two or all of them is used. As described above, in the liquid substance, as a result of adding new properties to the water by the present apparatus, a favorable phenomenon such as a sufficient dissolution of oxygen or ozone, an increase in permeation force, and the like occur, and these are stably produced. The feature is that it is retained. In the implementation, appropriate containers and supply equipment can be used to deal with the situation of the target, and large-scale targets can be supplied directly and continuously from this device.
(Ml) 植物の灌水に、 上記 (M0)記載の微小気泡含有液状物を使用 する。 当該液状物は通常の水よりも地面に浸透し易く、 かつ十分な酸素 又は活チ生酸素が安定に保持され、 徐々に放出されるため、 植物に対し迅 速に且つ長時間にわたって酸素又は活性酸素を供給することが出来る。 このことは植物の健全な生育と病害の予防 ·回復に顕著な効果を与え る。 液体として使用される水に植物に有益な微量要素その他の添加物を 加え、 更に有効なものとすることも出来る。 その他の特記事項は前項(Ml) The microbubble-containing liquid described in (M0) above is used for watering a plant. The liquid material permeates the ground more easily than ordinary water, and a sufficient amount of oxygen or active oxygen is stably retained and released gradually, so that the oxygen or activity of the plant can be increased quickly and for a long time. Oxygen can be supplied. This has a remarkable effect on healthy plant growth and disease prevention and recovery. Water used as a liquid contains trace elements and other additives that are beneficial to plants. In addition, it can be more effective. See the previous section for other special notes
(M0) 記載の通りである。 (M0) As described.
(M2) 水耕栽培において酸素供給の目的で水耕液中に気泡を導入す る場合、 上記 (M0)記載の微小気泡含有液状物を使用する。 液体として 使用される水に植物に有益な微量要素その他の添加物を加え、 更に有効 なものとすることも出来る。 その他の特記事項は上記 (M0) 記載の通 りである。  (M2) When bubbles are introduced into the hydroponic solution for the purpose of supplying oxygen in hydroponics, use the liquid containing microbubbles described in (M0) above. Water used as a liquid can also be made more effective by adding trace elements and other additives beneficial to plants. Other special remarks are as described in (M0) above.
(M3) 水質浄化のための藻類 ·菌類の代謝抑止、 殺菌等を目的とし て空気、酸素、 オゾン等を気泡の形で水中に供給する場合に、 上記 (M0) 記載の微小気泡含有液状物を使用する。 当該液状物は適宜な方法により 対象とする水中に供給されると、 通常の空気吹き込み等と異なり、 気泡 が浮上 ·発散することなく、 層状となって水底を覆いつつ拡大し、 強い 浸透力によって水底の付着物を剥離'浮上させるとともに、 酸素又は活 性酸素の徐放 ·安定供給により長時間にわたり水質浄化機能を示す。 池 '河川等の水質浄ィ匕に対しては、 基本装置のみを使用することによって、 簡易且つ高効率な浄化作用を提供することが可能である。 すなわち、 給 液口が水中に浸漬するように架台等適宜の手段によって基本装置を設置 し、 軟質ビニル管等を用いて吸気口に水面上から空気を供給しつつ該基 本装置を作動させて水中に微小気泡を放出することにより、 上述のごと き従来の空気吹込みとは全く異なる水質浄化機能を発揮する。 この際、 簡単な補助機構により添加物として適宜の微生物又は薬剤或いは其の双 方を給液口に導入し、 水中汚泥の分解或いは凝固等の機能を付加 ·向上 することも出来る。 また、 海中等深度の大きい場合においては、ブイ · 筏等の水上係留物に吊り下げるなどの手段により基本装置又は本装置を 水面下の適宜な深さに保持し、 例えば赤潮等の有害生物の抑止に使用す ることが出来る。 その他の特記事項は上記 (M0) 記載の通りである。 この実施の形態については、 若干の実験を実施し、 その有用性を確かめ た。 以下にその実施例について説明する。 (M3) When air, oxygen, ozone, etc. are supplied into water in the form of air bubbles for the purpose of suppressing metabolism and sterilization of algae and fungi for water purification, the liquid containing microbubbles described in (M0) above Use When the liquid material is supplied into the target water by an appropriate method, unlike normal air blowing etc., bubbles do not float or diverge, expand in a layered manner covering the water bottom, and due to strong osmotic force It exfoliates and accumulates adhering substances on the bottom of the water, and exhibits a water purification function for a long time due to the slow release and stable supply of oxygen or active oxygen. It is possible to provide a simple and highly efficient purifying action for water quality purification of ponds and rivers by using only basic equipment. That is, the basic device is installed by an appropriate means such as a gantry so that the liquid supply port is immersed in water, and the basic device is operated while supplying air from above the water surface to the intake port using a soft vinyl tube or the like. By releasing microbubbles into the water, a water purification function completely different from that of the conventional air blowing is exhibited as described above. At this time, appropriate microorganisms and / or chemicals can be introduced as additives into the liquid supply port by a simple auxiliary mechanism to add and improve functions such as decomposition or coagulation of submerged sludge. In addition, when the depth is large, such as underwater, the basic device or this device can be installed by means such as hanging from a mooring object such as a buoy or raft. It can be kept at an appropriate depth below the water surface and used to control pests such as red tide. Other special notes are as described in (M0) above. For this embodiment, some experiments were conducted to confirm its usefulness. The embodiment will be described below.
実施例 1 :直径 200mm、 長さ 700 mmの固定円筒を持つ基 本装置を水槽中に浸漬し、 1 HP 1500 r pmのモーターの駆動によ り装置内に空気と水とを容積比約 1 : 4の割合で導入し、 1 時間水槽内 の水を循環しつつ作動させた後、 槽内下部に生じた微細気泡を採取し、 レーザー光散乱により気泡径を測定した例では、 全気泡中直径 5〜10 μΐηのものが約 40%、 2〜3 mのものが約 20%であり、 密閉容器 中でこの状態が 20日以上持続することが観測された。  Example 1: A basic device having a fixed cylinder with a diameter of 200 mm and a length of 700 mm was immersed in a water tank, and the volume ratio of air and water was reduced to about 1 by driving a motor at 1 HP at 1500 rpm. : Introduced at a ratio of 4 and operated for 1 hour while circulating the water in the water tank. Then, the fine bubbles generated in the lower part of the tank were collected and the diameter of the bubbles was measured by laser light scattering. Approximately 40% of those with a diameter of 5 to 10 μΐη and about 20% of those with a diameter of 2 to 3 m, and it was observed that this state lasted for more than 20 days in a closed container.
実施例 2 :面積 1 50m2 :深さ lmの閉鎖池において、 固定円 筒の直径 15 Omm、 長さ 50 Omm、 駆動モーター 0. 5 HP、 15 00 r pmの基本装置 1台を使用し、 実施例 1と同様に水中に設置して 3週間連続運転を行い、 以下のような結果を得た。 Example 2: area 1 50 m 2 in the closed pond depth lm, using diameter 15 Omm fixed circular cylinder, length 50 Omm, the basic apparatus one drive motor 0. 5 HP, 15 00 r pm , It was installed in water and operated continuously for 3 weeks in the same manner as in Example 1, and the following results were obtained.
(1) 試験開始前、 池水は暗緑色に汚濁し、 悪臭があり、深さ 50 cmの点では白色物体の認知が困難であり、 池底には厚さ 10 cm前後 の汚泥が堆積していた。  (1) Before the test started, the pond water became dark green and had a bad smell.It was difficult to recognize a white object at a depth of 50 cm, and sludge with a thickness of about 10 cm was deposited on the bottom of the pond. Was.
(2) 試験開始 5時間後、 薄い油状膜が水面に浮上し始めた。  (2) Five hours after the start of the test, a thin oily film began to float on the water surface.
(3) 試験開始 1週間後、水面に池底汚泥と思われる物質が分散浮 遊し、 水の透明度が増加し、 白色の気泡層が基本装置を中心に水底を這 うように拡大していくのが認められ、 同時に稚魚の群れが水面近くを泳 ぐのが見られ始めた。  (3) One week after the start of the test, substances that seem to be pond bottom sludge disperse and float on the water surface, the transparency of the water increases, and the white bubble layer expands so as to crawl on the water bottom centering on the basic device. At the same time, schools of fry began to be seen swimming near the surface of the water.
(4) 試験開始 2週間後、 悪臭がほぼ消滅した。 ( 5 ) 試験開始 3週間後、 (3 ) に述べた浮遊物がほぼ消滅し、 汚 泥層の無い本来の池底が見え始めた。 (4) Two weeks after the start of the test, the odor almost disappeared. (5) Three weeks after the start of the test, the suspended matter described in (3) almost disappeared, and the original bottom of the pond without a sludge layer began to be seen.
( 6 ) 試験前後における水質分析の結果は表 1の通りである。  (6) Table 1 shows the results of water quality analysis before and after the test.
表 1  table 1
Figure imgf000023_0001
Figure imgf000023_0001
( 7 ) 試験開始前の浮遊物は殆どが藍藻類であり、 珪藻類は全く 見られなかったが、 3週間後の植物プランクトン分析結果では珪藻類の 著しい増加が見られた。 該分析結果を表 2に示す。 (7) Most of the suspended matter before the start of the test was cyanobacteria, and no diatoms were observed. However, phytoplankton analysis after 3 weeks showed a remarkable increase in diatoms. Table 2 shows the results of the analysis.
表 2  Table 2
綱 名 細胞数 Class name Cell count
¾¾ Oscillatoria sp. 280 渦鞭毛藻 Gimnodinium sp. 3,800 注 1¾ Cyclotella spp. 1,879,200  ¾¾ Oscillatoria sp. 280 Dinoflagellate Gimnodinium sp. 3,800 Note 1 ¾ Cyclotella spp. 1,879,200
その他 80,680 緑 藻 Pediastrum simplex 300  Others 80,680 Green algae Pediastrum simplex 300
Scendesmus acutus 400 稚魚の発生には、 これらの珪藻類が寄与しているものと考えられる。 実施例 3 :面積 4 5 h a、 水深 3 mの池において実施例 2と同様の 実験を 6 0日間行った結果、 開始前平均厚さ 5 0 c mあった池底のへド 口層は池全体にわったて消滅した。 また、 装置設置点近傍及ぴ設置点よ り 7 0 mの地点での硫化水素濃度は、 表 3に示す通り試験開始後 7日で 著しく減少した。 Scendesmus acutus 400 It is considered that these diatoms contribute to the occurrence of fry. Example 3: The same experiment as in Example 2 was performed for 60 days in a pond with an area of 45 ha and a depth of 3 m. As a result, the head layer at the bottom of the pond with an average thickness of 50 cm before the start was the entire pond. And disappeared. In addition, the hydrogen sulfide concentration near the installation point of the equipment and at a point 70 m from the installation point decreased remarkably 7 days after the start of the test as shown in Table 3.
表 3  Table 3
Figure imgf000024_0001
Figure imgf000024_0001
(M4) 魚類の飼育,繁殖に上記 (M0) 記載の微小気泡含有液状物 を使用する。 前項に述べたと同様の理由により、 簡便に長時間 ·安定な 酸素供給を行うことが出来,魚類の成育と病害の予防 ·回復に有効な効 果を与える。 その他の特記事項は上記 (M0) 記載の通りである。 (M4) Use the liquid containing microbubbles described in (M0) above for breeding and breeding fish. For the same reason as described in the previous section, it is possible to easily and stably supply oxygen for a long period of time, which has an effective effect on the growth of fish and prevention and recovery of disease. Other special notes are as described in (M0) above.
(M5) 水質保持を目的として上記 (M0)記載の微小気泡含有液状物 を水中に添加する。 既述の酸素供給機能により細菌の繁殖を防止し、 良 好な水質を保持することが出来る。 その他の特記事項は上記 (M0) 記 載の通りである。  (M5) The liquid containing microbubbles described in (M0) above is added to water for the purpose of maintaining water quality. The above-mentioned oxygen supply function can prevent bacterial growth and maintain good water quality. Other special remarks are as described in (M0) above.
(M6) 配管内面の保守に上記 (M0)記載の微小気泡含有液状物にお いて、 気泡が主として空気によって形成されるものを使用する。 既述の 浸透力と酸素供給作用とにより、 管内面のスケール除去と、 鉄管の場合 には赤鲭の除去と安定な黒鲭への転化の効果が齎される。 その他の特記 事項は上記 (M0) 記載の通りである。 安全技術における実施の形態 (M6) For maintenance of the inner surface of the pipe, use the liquid containing microbubbles described in (M0) above, in which bubbles are mainly formed by air. The aforementioned penetrating power and oxygen supply effect have the effect of removing scale from the inner surface of the pipe, and in the case of iron pipe, removing red and converting to stable black. Other special items are as described in (M0) above. Embodiment of safety technology
(NO) 安全技術の分野において、 消火剤或いは中和 ·吸収剤等とし て、 本装置によって製造し得る、 直径略 1 0 m以下安定な微小気泡を 含む微小気泡含有液状物を使用する。 当該液状物を形成する気体およぴ 液体には種種のものの使用が可能であるので、 目的に合わせてこれらを 選定して効率的な手段とすることが出来る。 気泡を含む液状物であるこ と力 ら、 気体のように拡散せず、 通常の液体に比べて展着性が高く局所 に滞留するため、 消火或いは中和 ·吸収の効率が良く、 微小気泡中の気 体が人体に有害な場合にも、 通常の気体としての使用に比べて安全性が 向上する。 当該液状物は適宜な容器及び供給装置によって対象の状況に 応じた簡便な使用が可能であり、 必要に応じて本装置から直接供給する ^とあ出来^。  (NO) In the field of safety technology, use microbubble-containing liquids containing stable microbubbles with a diameter of about 10 m or less that can be produced by this device as fire extinguishing agents or neutralizing / absorbing agents. Since various kinds of gases and liquids forming the liquid material can be used, these can be selected according to the purpose and used as an efficient means. Since it is a liquid containing bubbles, it does not diffuse like a gas and has high spreadability compared to ordinary liquids and stays locally, so fire extinguishing or neutralization / absorption efficiency is high, and Even if this gas is harmful to the human body, the safety is improved compared to the use as a normal gas. The liquid material can be easily used according to the target situation by using an appropriate container and a supply device, and is supplied directly from the device as needed.
(N1) 消火剤として、 上記 (NO)記載の微小気泡含有液状物におい て、 気泡が主として炭酸ガスによって形成されるものを使用する。 当該 液状物は炭酸ガスの微小気泡をふくむ水であるため、 炭酸ガスによる遮 断効果に併せて水による遮断効果及び燃焼物の温度低下効果が作用し、 高い消火機能を示す。 その他の特記事項については、 前項 (NO) 記載 の通りである。 産業上の利用の可能性  (N1) As the fire extinguisher, use is made of the liquid containing microbubbles described in (NO) above, in which bubbles are mainly formed by carbon dioxide gas. Since the liquid is water containing microbubbles of carbon dioxide gas, it has a high fire extinguishing function, with a water-blocking effect and a combustion-product temperature-lowering effect in addition to the carbon dioxide gas-blocking effect. Other special remarks are as described in the preceding paragraph (NO). Industrial potential
本発明にかかる製造方法により、 直径略 1 O m以下の安定した 微小気泡を含有する液状物を容易に且つ多種にわたり製造することが可 能となり、 その結果、 工業技術、 生活技術および安全技術の各分野にお いて多くの有用な製品或いは中間製品が提供される。  According to the production method of the present invention, it is possible to easily and widely produce a liquid material containing stable microbubbles having a diameter of about 1 Om or less, and as a result, industrial technology, living technology and safety technology can be produced. Many useful or intermediate products are provided in each area.

Claims

請 求 の 範 囲 界面活性剤を用いることなく、 固定筒の内部にモータにより回転す る回転筒を設置し、 該固定筒の一端付近には吸液口と吸気口とを設 け、 該固定筒の他端には該固定筒の外部に連通する連通室を設け、 該連通室内には該モータにより回転する送出手段を設け、 該送出手 段が連通室内の液体を外部に送出することにより連通室内と固定筒 内が負圧となって吸液口と吸気口とよりそれぞれ液体と気体とが固 定筒内に導入されるようにし、 更に、 固定筒の内周面と回転筒の外 周面とにそれぞれ断面がほぼ台形状の突条を該固定筒ないし回転筒 の長さ方向に複数本形成することによってこれら各突起間を断面が ほぼ逆台形状の溝とし、 各溝内部に永久磁石を配置した気液混合装 置を基本とした装置によって製造し得る、 液体中に形成された直径 略 1 0 / m以下の安定した微小気泡を含有する微小気泡含有液状 物。  Scope of request A rotating cylinder that is rotated by a motor is installed inside the fixed cylinder without using a surfactant, and a liquid suction port and an intake port are provided near one end of the fixed cylinder, and the fixed cylinder is fixed. A communication chamber communicating with the outside of the fixed cylinder is provided at the other end of the cylinder, and a sending means rotated by the motor is provided in the communication chamber, and the sending means sends the liquid in the communication chamber to the outside. Negative pressure is applied to the communication chamber and the inside of the fixed cylinder so that liquid and gas are introduced into the fixed cylinder from the liquid suction port and the suction port, respectively. By forming a plurality of ridges each having a substantially trapezoidal cross section on the peripheral surface in the longitudinal direction of the fixed cylinder or the rotary cylinder, a groove having a substantially inverted trapezoidal cross section is formed between the projections. Liquid that can be manufactured by a device based on a gas-liquid mixing device with a permanent magnet Substantially formed in a diameter 1 0 / m or less microbubble-containing liquid containing a stable microbubbles.
2. 請求の範囲 1に記載された微小気泡が主として空気によって形成さ れる微小気泡含有液状物。  2. A liquid containing microbubbles, wherein the microbubbles described in claim 1 are mainly formed by air.
3 請求の範囲 1に記載された液体が水又は添加物を含む水であり、 微 小気泡が主として空気によつて形成される微小気泡含有液状物。 3. A liquid containing microbubbles, wherein the liquid according to claim 1 is water or water containing an additive, and microbubbles are mainly formed by air.
4 請求の範囲 1に記載された液体が天然に存在する水 (河川水、 湖沼 水、 海水等) 又はこれに添加物を加えたものであり、 微小気泡が主 として空気によって形成される微小気泡含有液状物。 4 Water in which the liquid described in claim 1 exists naturally (river water, lake water, seawater, etc.) or an additive added thereto, and microbubbles are mainly formed by air. Containing liquids.
5 請求の範囲 1に記載された微小気泡が主として水素によって形成さ れる微小気泡含有液状物。 5. A liquid containing microbubbles, wherein the microbubbles described in claim 1 are mainly formed by hydrogen.
6 . 請求の範囲 1に記載された微小気泡が主として酸素によって形成さ れる微小気泡含有液状物。 6. A liquid containing microbubbles, wherein the microbubbles described in claim 1 are mainly formed by oxygen.
7 . 請求の範囲 1に記載された微小気泡が主として窒素によって形成さ れる微小気泡含有液状物。  7. A liquid containing microbubbles, wherein the microbubbles described in claim 1 are mainly formed by nitrogen.
8. 請求の範囲 1に記載された微小気泡が主として炭酸ガスによって形 成される微小気泡含有液状物。  8. A liquid containing microbubbles, wherein the microbubbles described in claim 1 are mainly formed by carbon dioxide gas.
9 . 請求の範囲 1に記載された液体が水又は添加物を含む水であり、 微 小気泡が主として炭酸ガスによつて形成される微小気泡含有液状 物。  9. A liquid containing microbubbles, wherein the liquid according to claim 1 is water or water containing an additive, and microbubbles are mainly formed by carbon dioxide gas.
1 0 . 請求の範囲 1に記載された微小気泡が主としてオゾンによって 形成される微小気泡含有液状物  10. Microbubble-containing liquid material in which the microbubbles described in claim 1 are mainly formed by ozone
1 1 . 請求の範囲 1に記載された液体が水又は添加物を含む水であり、 微小気泡が主としてオゾンによつて形成される微小気泡含有液状 物。  11. The liquid according to claim 1, wherein the liquid is water or water containing an additive, and the microbubbles are mainly formed by ozone.
1 2 . 請求の範囲 1に記載された液体が油脂類であり、 微小気泡が主と して単一種又は複数種のアルコール蒸気によって形成される微小気 泡含有液状物。  12. A liquid containing microbubbles, wherein the liquid according to claim 1 is an oil or fat, and the microbubbles are mainly formed by a single kind or plural kinds of alcohol vapors.
1 3 . 固定筒の内部にモータにより回転する回転筒を設置し、 該固定筒 の一端付近には吸液口と吸気口とを設け、 該固定筒の他端には該固 定筒の外部に連通する連通室を設け、 該連通室内には該モータによ り回転する送出手段を設け、 該送出手段が連通室内の液体を外部に 送出することにより連通室内と固定筒内が負圧となって吸液口と吸 気口とよりそれぞれ液体と気体とが固定筒内に導入されるように し、 更に、 固定筒の内周面と回転筒の外周面とにそれぞれ永久磁石 を配置し、 以つて固定筒内に導入された液体に微細な気泡を混入さ せた状態で該液体を送出手段により外部に送出するようにした気液 混合装置において、 前記固定筒の内周面と回転筒の外周面とにそれ ぞれ断面がほぼ台形状の突条を該固定筒ないし回転筒の長さ方向に 複数本形成することによってこれら各突条間を断面がほぼ逆台形状 の溝とし、 前記永久磁石をこれら各溝内部に配置することを特徴と する気液混合装置。13 3. A rotating cylinder that is rotated by a motor is installed inside the fixed cylinder, a liquid suction port and an intake port are provided near one end of the fixed cylinder, and the outside of the fixed cylinder is provided at the other end of the fixed cylinder. A communication means is provided for communicating with the inside of the communication chamber, and a sending means rotated by the motor is provided in the communication chamber. The sending means sends the liquid in the communication chamber to the outside, so that the communication chamber and the inside of the fixed cylinder have a negative pressure. Liquid and gas are introduced into the fixed cylinder through the liquid suction port and the suction port, respectively. Further, permanent magnets are respectively provided on the inner peripheral surface of the fixed cylinder and the outer peripheral surface of the rotating cylinder. Wherein the liquid introduced into the fixed cylinder is mixed with fine bubbles, and the liquid is sent out to the outside by the sending means. By forming a plurality of ridges each having a substantially trapezoidal cross section on the surface and the outer peripheral surface of the rotary cylinder in the longitudinal direction of the fixed cylinder or the rotary cylinder, the cross section between these ridges is substantially inverted trapezoidal. Wherein the permanent magnet is disposed inside each of the grooves.
. 前記回転筒における各溝内に配置された永久磁石の表面から前記 突条の表面までの深さが、 前記固定筒における各溝内に配置された 永久磁石の表面から前記突条の表面までの深さよりも大きいことを 特徴とする請求の範囲 1 3の気液混合装置。The depth from the surface of the permanent magnet arranged in each groove in the rotary cylinder to the surface of the ridge is from the surface of the permanent magnet arranged in each groove in the fixed cylinder to the surface of the ridge. 13. The gas-liquid mixing device according to claim 13, wherein the depth is larger than the depth of the gas-liquid mixing device.
. 前記永久磁石を前記固定筒と回転筒とのいずれか一方における前 記溝内と、 該固定筒と回転筒との他方における前記突条の表面とに それぞれ配置することを特徴とする請求の範囲 1 3の気液混合装 . 前記永久磁石を前記固定筒と回転筒とにおける各突条の上面に配 置することを特徴とする請求の範囲 1 3の気液混合装置。The permanent magnet is disposed in the groove in one of the fixed cylinder and the rotary cylinder, and on the surface of the ridge on the other of the fixed cylinder and the rotary cylinder. The gas-liquid mixing device according to claim 13, wherein the permanent magnet is disposed on an upper surface of each of the protrusions in the fixed cylinder and the rotating cylinder.
. 前記固定筒内における吸液口及び吸気口の下流側に前記モーター により回転する攪拌棒を設置することを特徴とする請求の範囲 1 3 の気液混合装置。14. The gas-liquid mixing device according to claim 13, wherein a stirring rod rotated by the motor is installed downstream of the liquid suction port and the suction port in the fixed cylinder.
. 前記攪拌棒が永久磁石を備えていることを特徴とする請求の範囲 1 7の気液混合装置。18. The gas-liquid mixing device according to claim 17, wherein the stirring rod includes a permanent magnet.
. 前記永久磁石がネオジム又はジルコニウムを主材料とするもので あることを特徴とする請求の範囲 1 3〜1 6又は請求の範囲 1 8の 13. The method according to claim 13, wherein the permanent magnet is mainly composed of neodymium or zirconium.
. 前記攪拌棒がイオン発生手段を備えていることを特徴とする請求 の範囲 1 8の気液混合装置。The gas-liquid mixing device according to claim 18, wherein the stirring rod includes an ion generating means.
. 前記吸液口より微生物及ぴ Zまたはミネラル及ぴノまたはその他 の添加剤を適宜な装置により液体と共に導入することを特徴とする 請求の範囲 1 3〜 2 0の気液混合装置。The gas-liquid mixing device according to any one of claims 13 to 20, wherein microorganisms and Z or minerals and other additives are introduced together with the liquid from the liquid suction port using an appropriate device.
. 請求の範囲 1 3〜2 0の装置に、 目的に応じ必要な付加装置を結 合して形成される気液混合装置。 A gas-liquid mixing device formed by combining the device according to claims 13 to 20 with an additional device necessary for the purpose.
PCT/JP2003/001228 2002-08-16 2003-02-06 Minute air bubble-containing liquid matter and device for manufacturing the liquid matter WO2004016344A1 (en)

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