JP2024100632A - NANO-PLASMA PARTICLE WATER GENERATION DEVICE WITH APPLICATION OF MECHANISM OF SEA SALT PARTICLE GENERATION ON OCEAN SURFACE FOR GENERATING NANO-PLASMA PARTICLE WATER (0.15 TO 1.0 nm) IN DEVICE HOUSING, DISSOLVING PARTICLE IN LIQUID UNDER PRESSURE TO GENERATE FUNCTIONAL WATER - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a device for generating nano-plasma particle water (particle diameter of 0.1 to 1.0 nm) in a device housing.

SOLUTION: A nano-particle water generation device housing 1 comprises all of a spray chamber and air pressurization mixing chamber 11, a nano-particle water storage tank 12, and a settling tank 13 for particle diameters of 10 to 100 nm). The spray chamber and air pressurization mixing chamber includes an air circulation inlet and an air chamber 17, an air circulation control venturi partition wall 14 is provided between both, and a narrow space is formed by a partition plate and a division plate. In the space of the spray chamber and air pressurization mixing chamber, nano-particle water is spouted and the nano-particle water is dissolved in the storage tank 12 by a pressure fan. A nano-plasma particle generation device housing 2 includes an air compressor 35, and six special nozzle units provided in a nao-plasma generation chamber 34. These construct a device for generating nano-plasma particle water. A water tank for storing nano-plasma particle water is provided below the housing.

SELECTED DRAWING: Figure 1

COPYRIGHT: (C)2024,JPO&INPIT

Description

The nano-plasma particle water (particle size 0.1-1.0 nm) of the present invention is a nano-plasma particle water generating device that utilizes the mechanism in which ultrafine particles such as ultrafine water particles, carbon dioxide gas, aerosol particles, and dust particles in the atmosphere, which float on the ocean surface, are dissolved in seawater due to the pressure difference of the water vapor partial pressure, and the components in the atmosphere are taken into the water liquid due to the pressure difference, etc., and nano-fine particle water is mixed into the device to produce functional water. This mechanism is greatly affected by the seawater temperature on the earth. In the vicinity of the equator where the seawater temperature is high, ultrafine particles such as carbon dioxide move from the seawater to the atmosphere, while in the northern and southern hemispheres where the seawater temperature is low, the ultrafine particle components are dissolved in seawater due to the difference in partial pressure of the components such as carbon dioxide gas and the pressurized pressure. This mechanism has the characteristic that the ultrafine particle components floating on the ocean surface coagulate and adsorb with the membrane-like sea salt film particles. This is because waves are always generated and broken on the sea surface where the wind blows, causing sea spray. However, these quickly fall due to gravity. The sea salt particles are generated when air is caught in the sea when the crests break, and bubbles burst on the sea surface. The diameter of the membrane-like film particles generated here is said to be about 0.1 to 10 μm. The mechanism of sea salt particle generation allows film particles and unit liquid layers to be generated and constructed. The mechanism of sea salt particle generation and its effects have been clarified through experiments by many scientific researchers, including Wood Cock. It has now become clear that approximately 40% of the carbon dioxide generated in the atmosphere around the world is dissolved in seawater.

The current water atomization technology in Japan and the world is the liquid nanobubble technology. Currently, the Ministry of Economy, Trade and Industry, companies, universities, research institutes, etc. are working to accumulate unique technologies and to internationally standardize them. This innovative technology product is a very wide-ranging technology that can be used in a wide range of fields, including agriculture, medicine, food, and infrastructure. On the supply side, this technology-related industry involves many companies such as manufacturing equipment manufacturers, manufacturing parts manufacturers, measuring instrument manufacturers, and engineering companies, and on the demand side, it has a cross-sectoral characteristic with many applications related to civil engineering, medicine, medicine, cosmetics, semiconductors, food, and even agriculture, forestry, and fisheries. The industry that both supplies and demands the technology (fine bubble industry) is thought to have the potential to become a core industry representing Japan in the future, like automobiles and home appliances, and even a future-oriented industry with a large market worldwide. The current technology for generating extremely small particle diameters, the ultimate density number, high dissolved oxygen concentration, etc., has low values and does not have a significant effect, so it has not spread. From now on, the establishment of further stable generation technology, etc. is urgently needed.

Considering the development history of nanobubble technology originating in Japan, microbubbles are bubbles with a diameter of 50 μm or less when they are generated. While normal bubbles rise rapidly in the water and burst at the surface and disappear, microbubbles shrink in the water and eventually disappear, "completely dissolving". Among them, the generation of free radicals and their survival as nanobubbles when they disappear in the water are important. Free radicals have excellent decomposition properties for chemical substances, so they can be used for water treatment, for example. On the other hand, they are extremely small bubbles of 1 μm or less and exist in the water for a certain amount of time. In order to generate such nanobubbles efficiently, it is necessary to generate microbubbles in water containing a certain amount of electrolytes, float them in a natural state, or apply simple physical stimuli. This causes electrolyte ions to accumulate in high concentrations around the microbubbles during the shrinking process, which creates an effect of suppressing the dissolution inside the bubbles, resulting in the microbubbles being stabilized for a long time as extremely small bubbles. Nanobubbles can be recognized as beings that are losing their properties as bubbles, but on the other hand, they give water extremely interesting properties. They act as so-called functional water.

気液二相流旋回型マイクロバブル発生装置
一般的に利用されているマイクロバブルの発生手法であり、水流を起こして渦を発生させ、渦内に気体を巻き込み、この渦を崩壊させた時に気泡がバラバラに細分化する現象を利用している。渦の発生方法には多くの手法があり、多種類のマイクロバブル発生装置として市販されている。下記に示すのはその概念図である。これは配管の出口付近に傾斜のついた羽根を装着し、水流が通過するときに旋回流を発生させる。水流は気体を含んでおり、この渦流を崩壊させることでマイクロバブルを発生させる。渦流を崩壊させる方法としては、配管中の障害物を利用する場合もあるが一般的にはバルク水中に渦を放出する方法が利用されている。水槽内の水は止まった状態に相当するので、ノズル部から水槽内に吐き出された渦は瞬間的に崩壊する。これにより渦中の気泡は細分化されマイクロバブルになる。渦を作る方法としては、シャフトにプロペラを取り付けて管内で回転させる方法や、円筒もしくは卵状の容器内に水流を送り込み容器内での水流の回転半径を小さくすることで、強い渦流を発生させる方法などがある。ここで発生された気泡の粒径分布は３０μｍ前後を中心に最少４μｍと最大５５μｍに分布している。気泡個数は１ｍｌあたり３０００～５０００個位である。
下記に気液二相流旋回型マイクロバブル発生装置の粒径分布と概念図を示す。

The methods for generating nanobubbles currently available in Japan and their characteristics are described below.
Dissolution type microbubble generator. Gases such as oxygen dissolve in water. Although the amount of gas dissolved varies depending on the type of gas, the amount of gas dissolved increases in proportion to the pressure as a basic characteristic. The pressurized dissolution type microbubble generation method utilizes this characteristic, and after dissolving a sufficient amount of gas in water at a certain level of high pressure, the pressure is released to create a supersaturated condition for the dissolved gas. This makes the excessively dissolved gas unstable, and the gas molecules in the supersaturated part try to jump out of the water. As a result, a large amount of bubbles are generated in the water. The basic system configuration uses a pump that can be driven by pressure to circulate the water in the water tank. At this time, water and gas are taken in from the suction side. These are discharged into the water tank from the extrusion side, but a nozzle is attached to the tip, which becomes a flow resistance for the water flow, so the pressure on the extrusion side increases. The pressure is generally adjusted to about 3 to 4 atmospheres. A dissolution tank is installed in the extrusion side path, and the gas taken in during suction is effectively dissolved in the water. The particle diameter of the bubbles generated by this method has a central particle diameter of 10 μm, and the second peak shows a somewhat broad distribution. In the case of a pressurized dissolution type microbubble generator, the number of bubbles of 50 μm or less is several thousand per 1 ml. The conceptual diagram of a dissolution type micro/nano bubble generator is shown below.

Gas-liquid two-phase flow swirl type microbubble generatorThis is a commonly used method of generating microbubbles. It uses the phenomenon that a water flow is generated to generate a vortex, gas is entrained in the vortex, and when the vortex collapses, the bubbles break down into small pieces. There are many methods for generating vortexes, and many types of microbubble generators are commercially available. The conceptual diagram is shown below. In this method, an inclined blade is attached near the outlet of the pipe, and a swirling flow is generated when the water flow passes through. The water flow contains gas, and microbubbles are generated by breaking down this vortex. As a method of breaking down the vortex, an obstacle in the pipe may be used, but a method of releasing the vortex into the bulk water is generally used. Since the water in the water tank is equivalent to a stationary state, the vortex discharged from the nozzle into the water tank collapses instantly. This breaks down the air bubbles in the vortex into microbubbles. There are several methods for creating vortices, including attaching a propeller to a shaft and rotating it inside a tube, or sending a water current into a cylindrical or egg-shaped container to reduce the radius of rotation of the water current inside the container, thereby generating a strong vortex. The particle size distribution of the bubbles generated here is centered around 30 μm, with a minimum of 4 μm and a maximum of 55 μm. The number of bubbles is about 3,000 to 5,000 per ml.
The particle size distribution and conceptual diagram of a gas-liquid two-phase swirl type microbubble generator are shown below.

Currently, nanobubbles are used in applications such as oxygen nanobubbles and ozone nanobubbles, which are less than 100 μm in diameter and have a very long half-life of several months. Oxygen nanobubble water is known to have an activating effect on living organisms, while ozone nanobubble water has a strong bactericidal effect. Efforts are being made to utilize these nanobubbles in applications in fields such as medicine, food, and biology.

The first major characteristic of microbubbles is their self-pressurizing effect. Microbubbles have the property of shrinking in water and eventually disappearing. This phenomenon of disappearance in water gives microbubbles very interesting characteristics. One of these is the increase in internal pressure. Although this is only a calculation, it creates infinite pressure at the moment of disappearance. This characteristic also has a significant impact on the dissolution of gases in water, making it possible to dissolve gases at levels above the saturation concentration. This has important implications in engineering. Here, we will introduce phenomena related to the increase in internal pressure.

ノ上昇速度入れる。The rate at which microbubbles rise when they self-pressurize is a very important factor in considering their engineering applications. Therefore, microbubbles were introduced into a transparent rare-earth cell and observed under a microscope in the absence of internal convection. The obtained image data was imported into a computer and subjected to image analysis to determine the relationship between bubble diameter and rate of rise. The measurement data for air microbubbles in distilled water under the measurement conditions of room temperature and atmospheric pressure are shown below.

Enter the ascent speed.

Regarding the second characteristic of microbubbles, the rise in internal pressure, bubbles are captured by the gas-liquid interface, and the surface tension of water acts on the interface. Since surface tension acts to reduce the surface, the surface tension functions as a force to compress the gas inside a bubble with a spherical interface. The pressure rise inside a bubble relative to the environmental pressure can be theoretically calculated by the following Young-laplace formula: △p-=4σ/D △p is the degree of pressure rise, σ is the surface tension, and D is the bubble diameter. For a microbubble with a diameter of 10 μm, the pressure rise is about 0.3 atmospheres, and for a microbubble with a diameter of 1 μm, the pressure rise is about 3 atmospheres. Gas dissolves according to Henry's law, so the pressurized gas dissolves efficiently in the surrounding water. Figure 9 shows data on the actual shrinkage of microbubbles in water. Since an increase in pressure increases the dissolution rate of the gas, coupled with an increase in the non-surface area, the smaller the bubble, the faster it shrinks. And it eventually disappears in water.

件を実現している。湖や港などの閉鎖性水域の環境汚染の最大の要因の一つは低層部の酸素欠乏である。特に夏場においては温度成層が形成されて表層の酸素を含んだ水が低層部にまで循環しないため、低酸素や無酸素状態になる．このような環境下では好気的な生物が死滅すると共に還元的な状況になって底泥などから栄養塩や重金属類の溶出が始まる。マイクロバブルは効率的に気体を溶解させるため、水環境の改善や化学工学などの分野において有効な手法となる。Regarding the increase in the concentration of dissolved gas in microbubbles, the increase in the internal air pressure of microbubbles, the "self-pressurizing effect," is important for the purpose of dissolving gas. In normal bubbling, there is a saturation pressure related to the environmental pressure when dissolving gas. In an atmospheric pressure environment, gas does not dissolve beyond the amount of dissolution corresponding to one atmosphere. However, in the case of microbubbles, the pressure inside the bubbles is higher than the environmental pressure, so the amount of gas dissolved in the water exceeds the supersaturation condition slightly more than expected from the atmospheric pressure. This is because in a water tank, the exchange of gas on the surface is determined by the atmospheric pressure, but the dissolution of gas inside is influenced by the condition of the microbubbles. Note that this saturation level is not extremely large, and the value is determined by the balance with the particle size distribution of the bubbles. In other words, since microbubbles floating in water vary in size, microbubbles smaller than a certain level dissolve gas into the water as they shrink, but bubbles larger than that level conversely take in the gas dissolved in the water and begin to grow into larger bubbles. The amount of dissolved gas is determined by these balances.

This has achieved the above results. One of the biggest causes of environmental pollution in closed waters such as lakes and harbors is a lack of oxygen in the lower layers. Particularly in the summer, temperature stratification occurs and the oxygen-containing water at the surface does not circulate to the lower layers, resulting in hypoxic or anoxic conditions. In such an environment, aerobic organisms die and the water becomes reductive, causing nutrients and heavy metals to begin eluting from the bottom mud. Microbubbles efficiently dissolve gases, making them an effective method for improving the water environment and in fields such as chemical engineering.

In addition, when considering the engineering application of microbubbles, the most interesting phenomenon is the generation of free radicals when the bubbles disappear, and their persistence as extremely small bubbles. Although these are contradictory phenomena, the concentration of surface charges is involved in the mechanism of action.

It has been known for over 50 years that bubbles in a solution are electrically charged, but the details are unknown and no systematic research has been conducted. The main reason for this is the difficulty of measurement. However, today, accurate analysis is possible by using electrophoretic methods. As a result, the engineering implications of bubbles being electrically charged are important. Even if extremely dense microbubbles are generated, the bubbles do not coalesce and reduce the bubble concentration because of the electrostatic repulsive force. It is also expected to have the effect of attracting pollutants and metal ions to the surface by electrostatic attraction.

As mentioned above, there are many types of microbubble generating devices in Japan today, and they are commercially available. However, all of them are devices that are used in liquid. As a result, the bubble particle diameter is around 0.15 μm, and the number of bubbles per 1 ml is said to be about 800 million. From these obtained values, the characteristics and properties of water and nano water technology are still not fully understood, so we believe that this technology has great potential. Based on the above, taking into account the values obtained with current technology, it is said that the difference in fluid resistance in the atmosphere is very large, about 19 times, and we believe that there is a limit to how much the current method can improve the values further.

International Publication No. 2005/030649 (WO, A1) JP 2005-246294 (JP, A) JP 2005-246293 (JP, A) JP 2004-121962 (JP, A) JP 2003-334548 (JP, A) JP 2003-245662 (JP, A) JP 2001-225060 (JP, A) JP 2001-009463 (JP, A) JP 09-276675 (JP, A) JP 07-060088 (JP, A) Hirofumi Ohnari, Part 1: Exploring the Appeal and Technical Potential of Microbubbles, 28th Multiphase Flow Lecture Series: The Appeal of Microbubbles and Their Application Technology, Japan, Japan Society of Multiphase Flow, June 2003. Masayoshi Takahashi, National Institute of Advanced Industrial Science and Technology Research on microbubbles and nanobubbles.

Non-patent item 3

Norihiro Amano: Air purification technology using nano-particle water in the atmosphere.

Conventional nanobubble generators currently being developed and manufactured in Japan generate particles with a diameter of 0.15 microns (150 nm) and a number density of 0.14%, both of which are very low values, limiting the scope of application of current technology. Furthermore, Japanese scientists do not pursue new technologies based on past technology. They do not seek change from the status quo and do not try to break away from the status quo. This technology was developed to break away from these issues.

The performance figures for conventional nanobubble generators are said to be an average particle size of 0.15 μm, the smallest value for particle size distribution devices that measure particle diameter. The density number is approximately 400 to 800 million particles per ml.

Another important characteristic of nanobubbles is the self-pressurizing effect. This function works as a force compressing the gas inside the bubbles due to the surface tension of the bubbles with a spherical interface. For example, it is said that the self-pressurizing force of a bubble with a diameter of 1 μm acts on the pressure collapse of about 3 atmospheres.

The self-pressurizing force described in [0007] above is said to cause the movement of ultrafine water particles in the liquid to behave in an astronomical manner. From examples of actual use, for example, examples where it is effectively used in water purification treatment have been reported. This action is thought to be due to the destruction pressure generated by the self-pressurizing force, which has a sterilizing effect on E. coli, mold, and general bacteria.

With regard to the performance values of conventional nanobubble generators, it is considered technically difficult to reduce the particle diameter to 0.15 μm or less, taking into account the loss resistance within the liquid.

Conventional nanobubble generators often use a method of drawing in air from the atmosphere via a pump or pressurizing it into the device in order to dissolve oxygen in the liquid. It is considered difficult to maintain a high dissolved oxygen concentration using conventional methods.

In view of the above-mentioned conventional drawbacks, the present invention aims to provide a generation device that generates nanoparticle water in the atmosphere and dissolves the nanoparticle water in a liquid together with air that contains the nanoparticle water, thereby making it possible to minimize the size of nano-fine particle water, significantly increase the density number, and maintain a high dissolved oxygen concentration.

The present invention makes it possible to rationally construct a more revolutionary device by applying the mechanism of the natural world in which components such as atmospheric aerosol particles on the ocean surface are dissolved and dissolved in ocean water by the mechanism of waves. It is possible to purify the atmospheric space as one application example by spraying nano-plasma particle water (0.1 to 1.0 nm particle size) in the atmospheric space, adsorbing and immobilizing the aerosol particles present in the atmosphere with the nano-particle water, and dissolving the fine particle water immobilized in the nano-plasma particle water (0.1 to 1.0 nm particle size) in an aqueous solution as contaminated water. The major features of the device of the present invention are that it is possible to rapidly generate a large amount of nano-particle water (1.0 nm particle size) and nano-plasma particle water (0.1 to 0.5 nm particle size) and to maintain a high concentration of dissolved oxygen for a long period of time.

The housing 1 of the device of the present invention is a housing that combines a spray chamber/air pressure mixing chamber, a nanoparticle water storage tank, and a 10-100 nm particle size precipitation tank, and the spray chamber/air pressure mixing chamber is provided with an air circulation intake and an air chamber, and an air flow control Venturi partition is provided between the two, and a narrow space is formed by a partition plate and a partition plate. In the space of the spray chamber/air pressure mixing chamber, the nanoparticle water is blown out and dissolved in the storage tank by a pressurizing fan.

The housing 2 of the device of the present invention is equipped with an air compressor and six special nozzle units in the nano-plasma generation chamber. These constitute a device for generating nano-plasma particle water. At the bottom of the housing, there is a water tank for storing nano-plasma particle water (0.1 to 0.5 nm particle size).

Furthermore, the spray chamber/air pressure mixing chamber is provided with a spray nozzle for generating nanoparticle water (1.0 nm particle size) in the order of 7, 8, 9, depending on the amount to be generated. The nozzle is fixed to a metal fitting provided in the spray chamber/air pressure mixing chamber, and the nanoparticle water generating device system is characterized by having a sphere that generates nanoparticle water (1.0 nm particle size) by collision of the water sprayed from the nozzle at a position away from the tip of the nozzle.

れ、且つ長時間維持していることが計測できた。この値は従来技術の約２～３倍にあたる。As is apparent from the above description, the effects obtained from the device of the present invention are as follows:
(1) Using a particle size distribution analyzer to analyze the size of nanoparticle water, we were able to generate particle sizes for each particle size distribution of 0.1-0.5 nm, 1.0 nm, and 1-5 nm, which is approximately 1/1500th of the size of the conventional technology. (nm is the unit of measurement, an abbreviation of nanometer.)
(2) By measuring the density and number of ultrafine water particles, a value of 10,000 trillion particles per milliliter was obtained, which is approximately 15 million times higher than conventional technology.

This value is about two to three times that of conventional technology.

Schematic diagram of the best device for carrying out the present invention Figure 1. Nano-plasma particle water (0.1-0.5 nm particle size) and nano-particle water (1.0 nm particle size) generating device Particle size distribution diagram generated by the nano-plasma particle water device of the present invention.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, an embodiment of the present invention will be described with reference to the drawings.

FIG. 1 shows the entire nanoparticle water (1.0 nm particle size) generator 1 and nano-plasma particle water (0.1-0.5 nm particle size) generator 2 of the present invention. The nanoparticle water generator 1 is made up of a bottom plate 52, front and rear side plates 50, left and right side plates 51, and a top plate 53, and is roughly a rectangular parallelepiped (ratio of plan to elevation is 2:4) with a regular square plan. The bottom is pyramidal, and an outlet for outlet piping is provided in the center to facilitate the discharge of nanoparticle water. The exterior is made up of these shapes.

The shape of the nano-plasma particle (0.1-0.5 nm particle diameter) generator housing ▲2 is effectively a horizontal cylindrical shape (with a cross-sectional to horizontal dimension ratio of 1:3). In order to effectively store nano-particle water on the bottom surface, the bottom is shaped to drop by about 50 mm. The pressure inside the generator housing ▲2 is maintained at 1.0 MPa using an air compressor ▲35. The nano-particle water (1.0 nm) generated in the nano-particle water (1.0 nm particle diameter) generator housing ▲1 is pumped through a nano-particle water piping to the nano-plasma particle (0.1-0.5 nm) generator housing ▲2 by a nano-particle water (1.0 nm) high-pressure pump. The nano-particle water (1.0 nm) maintained at a piping pressure of 7.0 MPa is discharged from six special nozzles inside the generator housing ▲2 and collided with three spheres at high speed. Nano plasma particle water (0.1-0.5 nm particle size) is reduced in pressure from 1.0 MPa to atmospheric pressure by a pressure reducing valve. The reduced pressure nano plasma particle water (0.1-0.5 nm) is sent to a nano plasma particle water storage tank via nano plasma particle piping and stored there. It is now possible to generate nano plasma particles (0.1-0.5 nm) with a 100% density of particles.

The nanoparticle water (1.0 nm particle size) generating device housing 1 takes in air into the spray chamber/air pressurized mixing chamber 11 by the pressurized blower fan 10, and in the spray chamber/air pressurized mixing chamber 11, the air rises along with the components in the nanoparticle water (particle size 1.0 nm) in the narrow space between the air/particle size control venturi partition plate 15 and the air/particle size control venturi partition plate 14, which is the side wall of the spray chamber/air pressurized mixing chamber 11, and meanders upward together with the nanoparticle water to the top, then flows downward through the narrow space provided between the air/particle size control venturi partition plate 16 and the air chamber 17. The role of the three partitions and three partition plates is to send 2.0 to 100 nm particle size water generated in the space and three side walls and top plate of the spray chamber/air pressurized mixing chamber 11 together with air to the air chamber via the air/particle size control venturi partitions/partitions 14, 15, and 16 described above. The water is then precipitated in the precipitation tank 13. The entire device is capable of generating nanoparticle water (1.0 nm) and nano plasma particles (0.1 to 0.5 nm) at a number density of 100%, which is a major feature of the device of the present invention.

Nanoparticle water is generated by impacting the three impact objects with high-pressure water ejected from special nozzles 7, 8, 9, etc. fixed to the side panel inside the housing 1 of this device. Nanoparticle water and dissolved oxygen are dissolved in the nanoparticle water storage tank 12 due to the difference between the pressurized dissolution and the partial pressure of water vapor, and nanoparticle water is generated.

At the upper middle part of the spray chamber/air pressurized mixing chamber 11 of the nanoparticle water generating device housing 1 in Fig. 1, a water supply pipe 6 is provided from the side wall, and special nozzles 7, 8, and 9 are formed at the tip thereof.

The high-pressure nanoparticle water pipe 21 is attached to the cylindrical longitudinal side plate of the nano-plasma particle (0.1 to 0.5 nm particle diameter) generating device housing 2 in FIG. 1 from the middle part of the side wall, and has six special nozzle units formed at its tip.

The current nanoparticle water technology is a technology originating in Japan that is being tackled by the domestic industry, government, and academia. The scope of use of the technology of the present invention can greatly contribute to decarbonization, and the synthesis technology with oil is particularly promising. In the agricultural field, it has been confirmed that it improves oxygen concentration and promotes the growth of vegetables, etc. In the medical field, it is used in eye drops, medicines, skin medicines, and organ medical regeneration technology, and in the food field, it has already been partially put into practical use in beverage extraction, wastewater purification, food cleaning, and food emulsions. In addition, it has a wide range of uses, such as sludge treatment equipment in the civil engineering field, cosmetics-related, semiconductor-related, and fishery-related, and research and development is progressing in each of them, and some products have been put into practical use. The particle diameter that can be generated from the device of the present invention is 0.1 to 10 nm (100% generation number density), and it has become possible to provide a device with significantly different performance from the conventional one. It is a device that can be applied over a wide range of industries.

▲1▼ Nanoparticle water (1.0 nm particle size) generator housing ▲2▼ Nano plasma particle (0.1 to 0.5 nm particle size) generator housing ▲3▼ Water storage tank ▲4▼ Water supply pipe ▲5▼ High pressure water pump ▲6▼ High pressure water supply pipe ▲7▼ Special nozzle 01-04
▲8▼ Special nozzle 02-05
▲9▼ Special nozzle 03-06
▲10▼ Air supply blower ▲11▼ Spray chamber and air pressurized mixing chamber ▲12▼ Nanoparticle water (1.0 nm particle size) storage tank ▲13▼ 10-100 nm particle size precipitation tank ▲14▼ Air particle size control Venturi partition ▲15▼ Air particle size control Venturi middle partition plate ▲16▼ Air particle size control Venturi partition ▲17▼ Air chamber ▲18▼ Air supply pipe ▲19▼ Nanoparticle water (1.0 nm particle size) piping ▲20▼ Nanoparticle water (1.0 nm particle size) high pressure pump ▲21▼ High pressure nanoparticle water (1.0 nm particle size) piping ▲22▼ Special nozzle unit 04
▲23▼ Special nozzle unit 05
▲24▼ Special nozzle unit 06
▲25▼ Special nozzle unit 07
▲26▼ Special nozzle unit 08
▲27▼ Special nozzle unit 09
▲28▼ Sphere 01
▲29▼ Sphere 02
▲30▼ Sphere 03
▲31▼ Nano plasma particle water (0.15-0.5 nm) piping ▲32▼ Pressure reducing valve ▲33▼ Nano plasma particle water (0.15-0.5 nm particle size) storage tank ▲34▼ Nano plasma generation chamber ▲35▼ Air compressor (high pressure air generator)
▲36▼ High pressure air supply pipe ▲37▼ 10-100 nm particle water discharge valve ▲38▼ Primary water supply pump ▲39▼ Primary water supply pipe filter ▲40▼ Primary water supply pipe ▲41▼ Nano plasma particle water storage tank 50 Front and rear side panels 51 Left and right side panels 52 Bottom panel 53 Top panel

Claims (14)

The device of the present invention dissolves carbon dioxide gas, aerosol particles, oxygen, and other substances in the atmosphere, which are ultrafine particle components floating on the ocean surface, in seawater on the ocean surface. The mechanism is to generate waves on the ocean surface caused by wind power, etc., and simultaneously generate sea salt particles (1.0 to 10. μm in diameter) using the energy of the waves, and purify the ultrafine particle components floating on the ocean surface with the energy of the sea salt particles. The device 1 of the present invention incorporates this law of nature. The components in the atmosphere are dissolved in an aqueous solution (meaning an aqueous solution with an electrical conductivity of 300 μs/cm or more containing electrolyte ions of iron, manganese, calcium, sodium, magnesium ions, and other minerals), and the aqueous solution is used to generate nano-plasma particles (0.1 to 0.5 nm in diameter) and nanoparticle water (1.0 nm in diameter), which becomes a special functional water. The main components of the device of the present invention are the nanoparticle water (1.0 nm in diameter) generation device housing ▲1. The main parts are: Nano plasma particle (0.1-0.5 nm) generator housing ▲2▼, water storage tank ▲3▼. Nano plasma particle water (0.1-0.5 nm particle size) storage tank ▲32▼. High pressure water pump ▲5▼. Nano particle water (1.0 nm particle size) high pressure pump ▲20▼. Air compressor ▲35▼. The nano particle water (1.0 nm particle size) generator housing ▲1▼ takes in air by ▲10▼ pressurized blower fan ▲10▼, which blows air into the spray chamber/air pressure mixing chamber ▲11▼. In the spray chamber/air pressure mixing chamber ▲11▼, nano particle water (particle size 1.0 nm) is sprayed, and the nano particle water (particle size 1.0 nm) is mixed with the components in the air and the nano particle water in the air pressure mixing chamber ▲11▼. In the air pressure mixing chamber ▲11▼, the nano particle water (1.0 nm) flows along the flow of the air taken in due to the pressure difference between the pressure and the water vapor pressure. The air that rises from near the bottom of the air/particle size control Venturi partition wall 14, which is the side wall downstream of the air flow of the nanoparticle water (1.0 nm particle size) generating device housing 1, to the narrow space between the air/particle size control Venturi partition plate 15, rises to the top together with the nanoparticle water, reaches the top, and then flows downward through the narrow space provided between the air/particle size control Venturi partition wall 16 and the air chamber 17. The role of the three partition walls and partition plates 14, 15, and 16 is to send the 2.0 to 100 nm particle size water generated in the space and the three side walls and top plate of the spray chamber/air pressurized mixing chamber 11 to the air chamber together with the air via the air/particle size control Venturi partition wall/partition 14, 15, and 16 described above. Then, it is precipitated in the precipitation tank 13. The entire device is capable of generating nanoparticle water (1.0 nm) and nano-plasma particles (0.1-0.5 nm) at a number density of 100%. In addition, the nanoparticle water (1.0 nm) and nano-plasma particles (0.15-0.5 nm) are functional waters that do not condense (freeze) until temperatures reach -30°C (Celsius), which is a major feature of the device of the present invention. The nano-plasma particle (0.1-0.5 nm particle diameter) generating device housing 2 of the present invention maintains the pressure inside the generating device housing 2 at 1.0 MPa using an air compressor 35. The nano-particle water (1.0 nm particle diameter) generated in the nano-particle water (1.0 nm particle diameter) generating device housing 1 is pumped by a nano-particle water (1.0 nm) high-pressure pump 20 to the nano-plasma particle (0.1-0.5 nm) generating device housing 2 via a nano-particle water piping 21 at a piping pressure of 7. Nanoparticle water (1.0 nm) maintained at 1.0 MPa is discharged from special nozzles 22, 23, 24, 25, 26, and 27 in the generator housing 2, and collides with the balls 28, 29, and 30 at a flow rate of 1000 m/hour, thereby generating nano-plasma particles (0.1 to 0.5 nm). The nano-plasma particle water (0.1 to 0.5 nm particle diameter) generated in the generator housing 2 is reduced in pressure from 1.0 MPa to atmospheric pressure by the pressure reducing valve 32. The reduced pressure nano-plasma particle water (0.1 to 0.5 nm) is sent to the nano-plasma particle water (0.1 to 0.5 nm particle diameter) storage tank 32 via the nano-plasma particle piping 31 and stored therein. This is a major feature of the device of the present invention, which makes it possible to generate nano-plasma particles (0.1 to 0.5 nm) at a number density of 100%. The process of generating nanoparticle water (1.0 nm particle size) in the nanoparticle water (1.0 nm particle size) generating device housing ▲1 of the present invention will be described. Water is stored in the water storage tank ▲3. Water is supplied from the high-pressure water pump ▲5 to the special nozzles ▲7, ▲8, and ▲9 configured inside the nanoparticle water (1.0 nm particle size) generating device housing ▲1▼ using the high-pressure water supply pipe ▲6▼ through the water supply pipe ▲4▼. The pressure is maintained at 7.0 MPa, and the nanoparticle water (1.0 nm) is generated by colliding with the special ball at a high speed of 500 km per hour via the special nozzles ▲7, ▲8, and ▲9, which is a major feature of the present invention. The special nozzles used in the special nozzle units 22, 23, 24, 28, 29, 30 installed in the spray chamber and air pressurized mixing chamber ▲11 of the nanoparticle water (1.0 nm particle size) generating device housing ▲1 of the present invention device have a cone shape with an inner diameter of 0.02 to 0.1 mm, and the pressure (7.0 to 12 MPa) from the special nozzles collides with the balls 25, 26, 27 at high speed, making it possible to generate nano-plasma particle water (0.1 to 0.5 nm particle size). This is a major feature of the present invention device. The special nozzles 7, 8, and 9 used in the nano-plasma particle (0.1-0.5 nm particle diameter) generating device housing 2 of the device of the present invention are cone-shaped with an inner diameter of 0.05-0.1 mm, and the pressure (7.0-12 MPa) from the special nozzles causes the balls 7-4, 8-5, and 9-6 to collide at high speed, making it possible to generate nanoparticle water (1.0 nm particle diameter). This is a major feature of the device of the present invention. The shape of the nanoparticle water (1.0 nm particle size) generator ▲1 of the present invention is a rectangular parallelepiped (ratio of plan and elevation is 2:4) and the plan is a regular square. The bottom is pyramidal, and an outlet for the outlet piping is provided in the center to facilitate the discharge of nanoparticle water. The material is stainless steel, which is a feature of the material and shape of the present invention's device from a comprehensive perspective in terms of corrosion resistance, long life performance, and ease of inspection. The shape of the nano-plasma particle (0.1-0.5 nm particle diameter) generating device housing ▲2 of the device of the present invention is effectively a horizontal cylindrical shape (with a cross-sectional to horizontal dimension ratio of 1:3). To effectively store nanoparticle water on the bottom surface, the bottom is shaped to drop down by about 50 mm. An outlet for outlet piping is provided at the bottom to facilitate the discharge of nano-plasma particle water. Stainless steel is the material that is characteristic of the material and shape of the device of the present invention from a comprehensive standpoint in terms of corrosion resistance, long life performance, and ease of inspection. The nanoparticle water (1.0 nm particles) produced by the device of the present invention has a particle count of about 1.0 nm per ml.

The above performance values indicate that the device of the present invention is capable of generating nanoparticle water (1.0 nm) as functional water. A major feature of the nanoparticle water (1.0 nm particle size) and nano-plasma particle water (0.15-0.5 nm particle size) generated by the device of the present invention is that the particle size distribution can be arbitrarily generated, for example, 0.1-0.3 nm, 0.3-0.5 nm, 1.0-2.0 nm, or 2.0-5.0 nm. In addition, for example, the particle diameter of 1.0 nm generated by this device generates a powerful pressure destruction energy when the bubble particles disappear. It is said that the force is the same as 300 atmospheres. For example, as one application, the great effect of this energy characteristic is that the sterilization and decomposition, coagulation and sedimentation ability of E. coli, mold, spores, general bacteria, inorganic matter, organic matter, etc. flowing into the wastewater purification tank is significantly improved. The effect is immeasurable. These effects result in a significant reduction in running costs due to the reduction in coagulants, separated chemicals, blower energy, etc. Another major feature of the device of the present invention is that it can be used as a substitute for disinfectants, pesticides, food, etc., and can be used to create safe and secure products that do not contain any chemicals. The main feature of the present invention's device is that it can stably generate nanoparticle water (particle size 1.0 nm) with a number density (100%) and nano-plasma particle water (0.1-0.5 nm) with a number density (100%). Number density (%) is a value that indicates the number of particles generated per volume. The technology for producing nanoparticle water (particle size 0.1 to 1.0 nm) of the present invention is characterized by the fact that nanoparticle water (particle size 0.28 to 1.0 nm) is produced by constructing a water supply pipe, a high-pressure pump, a special nozzle, and spheres into the device. The device of the present invention is characterized in that air transported from the suction chamber chamber ▲17 containing low-temperature, high-humidity air in the nanoparticle water (1.0 nm particles) generation device housing ▲1▼ via the air supply pipe ▲18▼ is supplied to the spray chamber/air pressurization chamber mixing chamber ▲11▼ by the air supply blower ▲10▼ for the purpose of pressurization and straightening. The spray chamber and air pressurized mixing chamber 11 for nanoparticle water (particle size 1.0 nm) made by the device of the present invention can store functional water at its bottom to any depth. The technology is characterized by storing an aqueous solution of 1.0 nm particle size (number density 100%) in a nanoparticle water (1.0 nm particle size) storage tank. By connecting multiple spray chambers and air pressure mixing chambers of this device, it is possible to control the distribution of nanoparticle water (particle size 1.0 nm) and nano-plasma particle water (particle size 0.15 to 0.5 nm) of functional water, which are measured and analyzed by a particle size distribution device that shows the performance of functional water. The number of particles is also measured.

A major feature of the device of the present invention is that it is an apparatus that makes it possible to