WO2023135829A1 - Hypochlorous acid gas generation structure, hypochlorous acid gas generation device, air conditioning system, and building - Google Patents

Hypochlorous acid gas generation structure, hypochlorous acid gas generation device, air conditioning system, and building Download PDF

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Publication number
WO2023135829A1
WO2023135829A1 PCT/JP2022/014784 JP2022014784W WO2023135829A1 WO 2023135829 A1 WO2023135829 A1 WO 2023135829A1 JP 2022014784 W JP2022014784 W JP 2022014784W WO 2023135829 A1 WO2023135829 A1 WO 2023135829A1
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hypochlorous acid
gas
cylindrical wall
water
mist
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PCT/JP2022/014784
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French (fr)
Japanese (ja)
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敏宏 松永
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株式会社Fmi
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    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61LMETHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L9/00Disinfection, sterilisation or deodorisation of air
    • A61L9/01Deodorant compositions
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61LMETHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L9/00Disinfection, sterilisation or deodorisation of air
    • A61L9/015Disinfection, sterilisation or deodorisation of air using gaseous or vaporous substances, e.g. ozone
    • A61L9/04Disinfection, sterilisation or deodorisation of air using gaseous or vaporous substances, e.g. ozone using substances evaporated in the air without heating
    • A61L9/12Apparatus, e.g. holders, therefor
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61LMETHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L9/00Disinfection, sterilisation or deodorisation of air
    • A61L9/14Disinfection, sterilisation or deodorisation of air using sprayed or atomised substances including air-liquid contact processes
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F8/00Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying
    • F24F8/10Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying by separation, e.g. by filtering
    • F24F8/108Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying by separation, e.g. by filtering using dry filter elements
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F8/00Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying
    • F24F8/20Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying by sterilisation
    • F24F8/24Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying by sterilisation using sterilising media
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F8/00Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying
    • F24F8/80Self-contained air purifiers
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters

Definitions

  • the present invention suppresses humidification of the space to be sterilized, releases only the hypochlorous acid gas in the gas phase that deactivates the virus from the hypochlorous acid water, and uniformly thins the space to be sterilized in a short time.
  • the present invention relates to a hypochlorous acid gas generating structure, a hypochlorous acid gas generator, an air conditioning system and a building capable of supplying concentrated hypochlorous acid gas.
  • the hypochlorous acid gas generator is equipped with a hypochlorous acid water storage tank at the bottom, has a double cylindrical wall of an outer cylindrical wall and an inner cylindrical wall, and has a lower portion of the outer cylindrical wall is immersed in hypochlorous acid water, the lower part of the inner cylindrical wall is separated from the hypochlorous acid water, the hypochlorous acid water is misted inside the inner cylindrical wall, and hypochlorous acid in the form of droplets Water is transmitted to the inner cylindrical wall and collected in the storage tank, and the mist, which is in a gas phase state, passes through the gap between the bottom of the inner cylindrical wall and the hypochlorous acid water surface of the storage tank, and flows between the double cylindrical walls. Raise the gap space of
  • hypochlorous acid gas generating structure, generator, air-conditioning system, and hypochlorous acid gas generating structure, generator, and air conditioning system that generate only gaseous hypochlorous acid gas without releasing liquid hypochlorous acid, which is feared to cause health hazards and metal corrosion. Regarding buildings.
  • Hypochlorous acid is a molecule made up of hydrogen atoms, chlorine atoms, and oxygen atoms bonded together, and exists in either a liquid phase or a gas phase at normal temperature and pressure.
  • hypochlorous acid water the state in which hypochlorous acid is dissolved in liquid water
  • mist the state in which hypochlorous acid is suspended in the air as fine droplets
  • hypochlorous acid in the gas phase state is called “hypochlorous acid gas”.
  • Mist with a size of 5 ⁇ m or less is included in hypochlorous acid gas in a gaseous state because it is vaporized instantaneously.
  • virus deactivation devices have been provided that emit mist generated from hypochlorous acid water into living spaces to deactivate airborne viruses and adhering viruses. Due to the pandemic of the new coronavirus (COVID-19), virus deactivation in living spaces has become an urgent issue, and virus deactivation equipment using hypochlorous acid has attracted strong interest compared to before the corona disaster. .
  • Patent Document 1 discloses a technology of a device that inactivates influenza viruses even at low humidity of 30% to 50% relative humidity by the present applicant. This technology suppresses humidification due to the generation of liquid droplets and liquid particles in order to deactivate airborne viruses with hypochlorous acid gas at low humidity that can suppress the growth of fungi.
  • hypochlorous acid solution is rotated and oscillated in a liquid state, and hypochlorous acid gas is generated by surface friction between the air in the air circulation unit and the hypochlorous acid solution, and the air intake is It is a device that introduces air and releases air containing hypochlorous acid gas due to the pressure difference between the air outlet and the air outlet, and releases hypochlorous acid gas while suppressing the amount of moisture released. .
  • hypochlorous acid water does not generate droplets or liquid fine particles.
  • hypochlorous acid gas generated is limited, and in addition to being able to inactivate the virus only in a small space, there was a problem that hypochlorous acid gas could not be diffused throughout the entire space in a short time. .
  • the present inventor conducted a test to confirm the relationship between the relative humidity of the space and the half-life period of hypochlorous acid gas in order to confirm the active period during which hypochlorous acid gas maintains its activity. .
  • Patent Document 2 a rotating cylindrical net body through which water and air can pass is provided, and the water collides with the inner wall of the net body to turn the water into mist, thereby increasing the surface area of the water and allowing it to pass through the processing chamber.
  • a negative ion generator for increasing the concentration of negative ions in the air to be treated.
  • the net body is rotated to blow air from above the space in which the water is turned into mist, toward the water surface, and the mist-laden air from the net body collides with the water surface. and is turned upside down to discharge the air from the discharge port.
  • the water surface is disturbed by the blown air, and many droplets are generated from the water surface.
  • the humidity of the air tends to be high.
  • Patent Document 3 discloses a technique for miniaturizing the main body of a negative ion generator. According to this technique, an inner cylinder is arranged concentrically in a cylindrical case, the case and the lower part of the inner cylinder are submerged, and a notch is provided in a part of the inner cylinder to form an inner cylinder. Air mixed with water mist generated in the inner cylinder is passed through the notch between the case and the inner cylinder through the notch, raised by a swirling motion, and released to the outside.
  • hypochlorous acid water When hypochlorous acid water is applied to the techniques described in Patent Documents 2 and 3, the relative humidity of the space to be sterilized is humidified to 60% or more, which is not suitable for the diffusion of hypochlorous acid gas. Hypochlorous acid mist in a liquid state could also diffuse into the space to be sterilized. Therefore, the applicant has developed a technology that generates only hypochlorous acid gas without generating hypochlorous acid water in the liquid phase state of droplets and liquid particles, and makes it difficult to increase the humidity of the released sterilization space. He devoted himself to the development and conceived of the present invention.
  • Patent Document 1 International Publication No. 2021-49045
  • Patent Document 2 JP-A-9-203540
  • Patent Document 3 JP-A-9-264574
  • the problem to be solved by the present invention is to suppress humidification of the space to be sterilized, release only the hypochlorous acid gas in the gaseous state that deactivates the virus from the hypochlorous acid water, and allow the space to be disinfected for a short time.
  • a hypochlorous acid gas generator, an air-conditioning system and a building capable of supplying hypochlorous acid gas having a uniformly low concentration.
  • a first invention of the present invention is a hypochlorous acid gas generating structure for generating only hypochlorous acid in a gaseous state
  • the hypochlorous acid gas generating structure comprises a storage tank of hypochlorous acid water
  • An outer cylindrical wall forming a double cylindrical wall includes a double cylindrical wall, a gas passage, an air pressurizing means, a hypochlorous acid water misting means, and a gas discharge port, and the storage tank and the lower part is immersed in the hypochlorous acid water, and the inner cylindrical wall forming a double cylindrical wall has a gap between the lower periphery and the hypochlorous acid water surface of the storage tank.
  • the storage tank penetrates the inside and outside of the outer cylindrical wall, and the air pressurizing means passes the gas from the gas inlet through the inside of the inner cylindrical wall.
  • the outside air is pressurized and guided to the discharge port, the misting means comprises a cylindrical mesh body and hypochlorous acid water diffusion means, and the mesh body rotates concentrically with the double cylindrical wall.
  • the diffusion means causes the hypochlorous acid water to collide with the net body inside the inner cylindrical wall to generate mist, and the hypochlorous acid water in a liquid phase is emitted inside the inner cylindrical wall.
  • the mist that is dropped and collected in the storage tank and becomes a gas phase is guided upward from the periphery of the gap to the gap space formed by the double cylindrical walls, and while the mist is rising,
  • the mist formed into droplets in the gap space is dropped and collected in the storage tank in the area of the gap space, and the gas discharge port is provided at an upper portion outside the region of the outer cylindrical wall, and from the gas discharge port, It is characterized by releasing only mist in gas phase and hypochlorous acid gas.
  • the hypochlorous acid water may be produced by dissolving sodium dichloroisocyanurate in water, or by electrolyzing an aqueous sodium chloride solution to generate slightly acidic hypochlorous acid water, and the manufacturing method is not limited.
  • Hypochlorous acid water has different properties depending on the pH, but pH 3.0 to pH 7.5 is suitable because hypochlorous acid gas with excellent virus deactivation effect is easily generated.
  • the hypochlorous acid water misting means is a cylindrical mesh and hypochlorous acid water diffusion means.
  • the dispersing means may immerse a funnel-shaped rotating body with an open bottom end in hypochlorous acid water, draw up the hypochlorous acid water by centrifugal force, and disperse it as droplets, and spray it by a spraying means. You may let The net body is preferably made of stainless steel so as to suppress corrosion, but the standard of the net body is not limited.
  • the air pressurization means By the air pressurization means, the air introduced from the outside air inlet is lowered toward the surface of the hypochlorous acid water in the inner cylindrical wall where the mist is generated.
  • the introduced air and the generated mist pass through the gap around the bottom of the inner cylindrical wall and the hypochlorous acid water surface, and are evenly introduced into the gap space between the outer cylindrical wall and the inner cylindrical wall and rise. be. Since the hypochlorous acid water surface outside the outer cylindrical wall is not disturbed because the entire circumference of the gap is raised evenly without being biased to a part of the gap.
  • the mist that did not become fine diameter becomes droplets and falls along the inner wall into the reservoir and is collected.
  • the fine mist rises evenly through the entire gap between the inner cylindrical wall and the outer cylindrical wall, but some of the mist becomes droplets in the process.
  • the droplets of mist adhere to the inner surfaces of the inner cylindrical wall and the outer cylindrical wall facing the gap, drop into a storage tank, and are collected. Since the gas discharge port is provided in the upper portion outside the region of the outer cylindrical wall, only fine mist reaches the gas discharge port without being affected by droplets caused by disturbance of the hypochlorous acid water surface.
  • mist and hypochlorous acid gas in gas phase means that it does not need to contain hypochlorous acid that is released in liquid phase, and of course the outside air is included. It's about.
  • the hypochlorous acid water is turned into mist, and the mist in the liquid state is recovered in the inner cylindrical wall and in the space between the inner cylindrical wall and the outer cylindrical wall. Then, only fine mist and hypochlorous acid gas, which are in a gaseous state, are discharged from the gas outlet provided outside the area of the outer cylindrical wall, which is not affected by droplets, into the space to be disinfected to deactivate the virus. I am releasing it.
  • only hypochlorous acid gas can be released in a larger amount than before while suppressing the humidification effect. As a result, even in a large space, it is possible to effectively generate hypochlorous acid gas that deactivates viruses in a short period of time.
  • a second invention of the present invention is a hypochlorous acid gas generator that generates only hypochlorous acid in a gas phase state, wherein the hypochlorous acid of the first invention It is characterized by having a gas generating structure. According to the second invention, since the hypochlorous acid gas generating structure of the first invention is configured in an integrated device, there is an effect that it can be easily moved and used.
  • a third invention of the present invention is the hypochlorous acid gas generator of the second invention, wherein the gas discharge port can be equipped with a first moisture release amount suppressing means, and the gas A water-repellent nonwoven fabric in which the path from the gas inlet to the gas outlet is airtight, and the first water release suppressing means has a fiber diameter of 1 ⁇ m or more and 30 ⁇ m or less and a pressure loss of 20 Pa or more and 60 Pa or less. It is characterized by being used as a filter.
  • Airtight from the gas inlet of the gas path to the gas outlet means that the gap between the main body and the lid of the device is airtight so that the mist in the liquid state does not leak.
  • the non-woven fabric filter may be attached either inside or outside the gas discharge port, but if it is attached inside, the mist that did not turn into gas becomes fine water droplets and easily falls into the water tank, which is preferable.
  • the non-woven fabric filter of the second invention has water repellency, has a fiber diameter of 1 ⁇ m or more and 30 ⁇ m or less, and is an easily available filter that satisfies the JIS standard.
  • an electrostatically treated non-woven fabric filter made of polyurethane resin, polyethylene resin, polypropylene resin, etc. used for general masks has a pressure loss of about 30 Pa, and depending on the water repellency and fiber diameter, the particle size If the mist is up to 2 ⁇ m, it can be removed at a rate of 98% or more, which is preferable. According to the third invention, only the hypochlorous acid gas can be efficiently released while the amount of water released is further suppressed.
  • a fourth invention of the present invention is the hypochlorous acid gas generator of the second invention, wherein the gas discharge port can be equipped with a second moisture release amount suppressing means, and the gas The path from the gas introduction port to the gas discharge port is airtight, and the second moisture release suppressing means includes hydrophobic nanofibers having a fiber diameter of 70 nm or more and 200 nm or less and a pressure loss of 20 Pa or more and 60 Pa or less. It is characterized by being used as a filter.
  • the gas outlet is provided with a nanofilter that serves as the second means for suppressing the amount of water released.
  • Hydrophobic nanofibers with a fiber diameter of 70 nm or more and 200 nm or less absorb and filter fine particles by Van der Waals force. Therefore, even substances of a size that cannot be removed by a non-woven fabric filter, for example, fine water particles with a particle diameter of 100 nm, and even solid particles such as chlorides can be removed.
  • the nanofilter is not limited to being composed only of nanofibers, and may be provided with nonwoven fabric forming a shape-retaining layer on both sides of the nanofibers.
  • the nanofilter may be used alone, or may be used in combination with the nonwoven fabric filter of the third invention.
  • Suitable materials for the hydrophobic nanofibers include, for example, polyurethane resins and polypropylene resins, since the diameter of the fibers can be easily reduced. According to the fourth invention, even solid particles such as chlorides can be removed, and the amount of moisture released can be further suppressed, and only gas in the gas phase is released from the hypochlorous acid gas generator. can be made
  • a fifth invention of the present invention is the hypochlorous acid gas generator of the second invention, wherein the gas discharge port can be equipped with a third moisture release amount suppressing means, and the gas The path from the gas inlet to the gas outlet is airtight, and the third moisture release suppressing means is a repellent fiber having a fiber diameter of 1 ⁇ m or more and 30 ⁇ m or less and a pressure loss of 20 Pa or more and 60 Pa or less from the upstream side.
  • a double filter consisting of a nonwoven fabric filter having water and a nanofilter containing hydrophobic nanofibers having a fiber diameter of 70 nm or more and 200 nm or less and having a pressure loss of 20 Pa or more and 60 Pa or less, and the distance between the double filters is at least 5 mm. or more.
  • the gas discharge port is provided with a double filter that serves as the third means for suppressing the amount of water released.
  • the nonwoven fabric filter forming a double filter is the same as the nonwoven fabric filter of the third invention, and the nanofilter is the same as the nanofilter of the fourth invention.
  • the maximum pressure loss is less than 120 Pa, which is about half the pressure loss of a HEPA filter, so it can be applied to large-capacity equipment. If a filter with low pressure loss is combined, gas can be discharged through a double filter even with a fan that has high air permeability and is used in a domestic gas generator.
  • the double filters are spaced apart by at least 5 mm, even if fine water adhering to the upstream surface of the non-woven fabric filter due to the pressure of the air pressurizing means, it may blow out between the double filters. Also, fine moisture is vaporized before reaching the nanofilter. According to the fifth invention, it is difficult for mist to clog the gaps of the nanofilter, and even if the gas generator is operated continuously for a long period of time, the amount of released water can be suppressed.
  • a sixth invention of the present invention is the hypochlorous acid gas generator according to the third to fifth inventions, wherein the upstream surface of the water release amount suppressing means attached to the gas discharge port is an inclined surface. None, the mist droplets on the upstream surface are dropped into the storage tank along the inclined surface.
  • the filter serving as the water release amount suppressing means is attached, the upstream surface of the filter is pressurized, and during long-term continuous operation of the apparatus, the mist that has not passed through the fine filter is deposited on the surface of the filter. It may become fine water droplets and adhere.
  • the upstream surface of the water release amount suppressing means forms an inclined surface, fine water droplets are easily turned into large droplets and are easily allowed to naturally fall along the inclined surface.
  • the moisture release amount suppressing means is a double filter, it is preferable to bend the upstream surface of only the non-woven fabric filter disposed on the upstream side, that is, on the storage tank side.
  • a seventh invention of the present invention is the hypochlorous acid gas generator according to the third to fifth inventions, wherein gas diffusion means for generating an air flow is provided outside the gas discharge port, and the gas is The diffusing means is characterized by diffusing the hypochlorous acid gas released from the gas outlet.
  • the filter makes it difficult for hypochlorous acid gas to be released, it tends to accumulate near the release port.
  • the hypochlorous acid gas having a short half-life period can be rapidly diffused, and the hypochlorous acid gas of high concentration can be diffused. It diffuses hypochlorous acid gas at a low concentration to every corner of a room with a large air volume, inactivating viruses in a short time and preventing metal corrosion.
  • An eighth invention of the present invention is an air conditioning system that generates only hypochlorous acid in a gaseous state and supplies it to a room in an air conditioning system, wherein the hypochlorous acid gas generating structure of the first invention is used for air conditioning.
  • the hypochlorous acid gas generating structure of the first invention is used for air conditioning.
  • only mist and hypochlorous acid gas in a vapor phase state are introduced into the fresh air introduction route into the room and supplied.
  • the air conditioning system should pressurize the air taken in from the outside with the air pressurization means and introduce it into the fresh air supply path.
  • a low humidity environment is provided, hypochlorous acid gas is supplied together with ventilation with fresh outside air, and deodorization and sterilization are performed in a state where the growth of fungi is suppressed, and the elderly and An unprecedented advantageous effect can be obtained that an air-conditioning system suitable for a medical care room can be provided.
  • a ninth aspect of the present invention is a building in which the air-conditioned area is divided into a plurality of compartments. It is characterized by having According to the ninth invention, since the air-conditioned area is divided into a plurality of compartments, hypochlorous acid gas, which has a virus-inactivating effect but has a limited half-life cycle, is effectively supplied to each compartment. There is an effect that it can be a building that
  • hypochlorous acid gas generating structure of the first invention is configured in an integrated device, there is an effect that it can be easily moved and used.
  • hypochlorous acid gas can be efficiently released while the amount of water released is further suppressed.
  • the fourth aspect of the present invention even solid particles such as chlorides can be removed, and the amount of water released can be further suppressed, and the gas phase state from the hypochlorous acid gas generator can be reduced. Only gas can be released.
  • the sixth aspect of the present invention even if the hypochlorous acid gas generator is continuously operated for a long time, the amount of gas generated is unlikely to decrease, and the gas can be stably and continuously released. can be done.
  • the hypochlorous acid gas with a short half-life period can be rapidly diffused, and the hypochlorous acid gas with a high concentration It diffuses hypochlorous acid gas at a low concentration to every corner of a room with a large air volume without causing chloric acid gas to be concentrated, inactivating viruses in a short time and preventing metal corrosion.
  • hypochlorous acid gas is supplied together with ventilation with fresh outside air, and deodorization, sterilization, etc. are performed in a state where the growth of fungi is suppressed.
  • the air conditioning system can be made suitable for the elderly and medical rooms, which is an unprecedented advantageous effect.
  • hypochlorous acid gas which has a virus inactivating effect but has a limited half-life cycle, can be effectively supplied to each section. play.
  • the hypochlorous acid gas generator (hereinafter referred to as the generator) is provided with a double cylindrical wall, the outer cylindrical wall forming the double cylindrical wall is erected from the storage tank, and the lower part is It was immersed in chloric acid water to provide a gap between the lower periphery of the inner cylindrical wall and the hypochlorous acid water surface.
  • the air introduced by the air pressurization means collides with the rotating net body of hypochlorous acid water to generate mist, and the mist descends in the inner cylindrical wall to create a double The gap space formed by the cylindrical wall is made to rise.
  • a gas discharge port is provided on the outside of the outer cylindrical wall where droplets from the chloric acid water surface do not fly, and only mist and hypochlorous acid gas (hereinafter referred to as gas) that are in a gas phase state are emitted.
  • the first test for confirming the properties of the gas and the second test using the device according to the present invention will be explained, and then the examples will be explained.
  • a “gas half-life period confirmation test” and a “first confirmation test of the correlation between the relative humidity and the amount of gas generated” were performed.
  • the second test using this device, "moisture release test”, “filter effect confirmation test”, “gas generation confirmation test”, “liquid phase mist absence confirmation test”, “influenza virus deactivation test”, A "second confirmation test of the correlation between the relative humidity and the amount of generated gas” was carried out.
  • a humidity control device and a gas generation device described in Patent Document 1 were installed in a test container having a volume of 1.2 m 3 .
  • the gas generator uses a small fan with an air volume of about 0.012 m 3 per minute.
  • hypochlorite was dissolved in purified water, chlorides were removed, and gas was generated from the hypochlorous acid water whose pH was adjusted to be weakly acidic.
  • the amount of hypochlorous acid water was 500 ml, and the effective chlorine concentration was adjusted to about 100 ppm.
  • the test room was set to a test environment of 20°C.
  • the generator was driven in the test container for 10 minutes. Measure the maximum available chlorine concentration in the test container after 10 minutes, and measure the time from reaching the maximum available chlorine concentration until the available chlorine concentration becomes 1/2 (hereinafter referred to as the half-life cycle), and at that time Final relative humidity was measured.
  • the test results are shown in Table 1 below and FIG. Note that the maximum effective chlorine concentration at each humidity is different.
  • the half-life period was the longest when the initial relative humidity was adjusted to 10%, and was about 38 minutes (see Table 1, a in Figure 2).
  • the half-life period gradually decreased as the initial relative humidity increased, and decreased to an initial relative humidity of 60%, at which time the half-life period was about 10 minutes (see f in Table 1 and Fig. 2).
  • the half-life period was 22 minutes (see Table 1, Fig. 2g).
  • the gas In a humid environment with a long half-life cycle of gas, the gas can be left to float in the space to be disinfected for a long time, so even if the gas concentration is low, the virus deactivation effect can be expected. It was confirmed that the relative humidity of the space to be sterilized, which has a long half-life cycle that facilitates maintenance of gas activity, should preferably not exceed 50% without excessive humidification of the space to be sterilized.
  • the gas concentration in the test container was 12.5 ppb when the relative humidity was 20%, which was the highest value (see i in Table 2 and Fig. 3).
  • the amount of gas generated gradually decreased with the same slope up to a relative humidity of 50%.
  • the amount of gas generated decreased, and at 70% relative humidity (see n in Table 2 and Fig. 3), it was about one-third that at 20% relative humidity. It was confirmed that the amount was significantly reduced.
  • the air pressurizing means of the apparatus is a sirocco fan with a blowing capacity of about 1.2 m 3 per minute and a pressurizing capacity of about 147 Pa.
  • gas was generated from hypochlorous acid water in which sodium dichloroisocyanurate was dissolved in water.
  • the amount of hypochlorous acid water used at one time was 3 L, and the concentration of hypochlorous acid water was about 100 ppm.
  • the second test was carried out by setting the room temperature to 22° C. in a reinforced concrete room with a floor area of about 55 m 2 and a volume of about 135 m 3 where only temperature control and ventilation were possible.
  • Example release test In the moisture release test, the generator 1 of Example 1 of the present invention was used, continuous operation was performed for 6 hours, and the amount of moisture released into the sterilization target space was confirmed from the remaining amount of water.
  • the moisture release test was conducted in four modes: no filter attached to the gas outlet, only a nanofilter attached, only a non-woven fabric filter attached, and a double filter attached.
  • a recommended rated humidification capacity of a humidifier is defined according to the applicable floor area.
  • the rated humidifying capacity is the humidifying capacity per hour at room temperature of 20° C. and humidity of 30%. Since the floor area of the test room is about 55 m 2 and the building is made of reinforced concrete, the rated humidifying capacity originally required for the humidifier is about 1200 mL/h. Table 3 below shows, as test results, the amount of water released for 6 hours, the humidifying capacity per hour, and the humidifying ratio with respect to the rated humidifying capacity.
  • the generator 1 has a humidification capacity of 215 mL per hour without a filter that suppresses the amount of water released, which is only 18% of the recommended rated humidification capacity. .
  • the humidification capacity per hour was 50 mL to 60 mL, which was 4% to 5% of the rated humidification capacity, and it was confirmed that only a very small amount of water was released.
  • FIG. 4(A) A filter effect confirmation test was conducted by changing the type of the filter 100 to confirm the difference in the influence of the released gas on the metal corrosive action (see FIG. 4(A)).
  • the gas outlet 31 of the generator 1 was covered with filters of different types, copper fibers 110 made of fine wires were placed, and differences in corrosion were confirmed.
  • a total of four tests were carried out, one in which the specimen was exposed to the air, and the other in which 100 ppm of hypochlorous acid water was used.
  • the test time for each test was 2 hours. The results of this test are shown in Table 4 below and in FIG. FIG. 4(A) shows a test state, and FIG. 4(B) shows a photograph of copper fibers.
  • Fig. 4(B) the specimens are arranged in order of least corrosion. No change was observed when the copper fibers were only exposed to the space (a in FIG. 4(B)).
  • a nanofilter was attached to the gas outlet and a copper fiber was placed on the nanofilter (b in FIG. 4(B))
  • the peripheral edge was discolored, but the metallic luster remained in other areas.
  • a non-woven fabric filter was attached to the gas discharge port and copper fibers were placed on the non-woven fabric filter (Fig. 4(B), c)
  • the overall color was dull and the metallic luster was lost.
  • a copper fiber was hung from the gas outlet without attaching a filter to the gas outlet (d in FIG. 4(B)), the entire surface turned black and had no metallic luster.
  • FIG. 5(B) The figures in Fig. 5(B) are arranged in descending order of metal corrosion.
  • the copper fiber (a in FIG. 5(B)) positioned directly above the gas discharge port was wholly blackened and lost its metallic luster.
  • the copper fibers separated from the gas outlet by 20 cm (b in FIG. 5(B)) had a slight discoloration at the peripheral edges and most of the metallic luster remained.
  • gas is generated from the gas discharge port, and the gas affects the metal directly above the gas discharge port, but if it is separated from the gas discharge port by 20 cm, the gas diffuses and the effect on the metal diminishes. , 40 cm or more, the gas diffuses widely, and it was confirmed that the influence on metal corrosion is small even without a filter.
  • FIG. 6(A) shows a test state
  • FIG. 6(B) shows a photograph of copper fibers.
  • a cylindrical hood part 300 with an open top is attached to the outside of the gas discharge port, the copper fiber a 310 is suspended inside the hood part, and the copper fiber b 320 is laterally protruded to a position away from the gas flow.
  • a tissue paper 330 was attached to the hood part so as to flutter along the wind (see FIG. 6(A)).
  • Hypochlorous acid water has a concentration of 100 ppm, and the capacity remains at 3 L.
  • the copper fiber b320 was positioned about 15 cm away from the hood.
  • tissue paper 330 which was flapping over the hood, did not get wet at all at all times, and that no liquid-phase mist was generated.
  • the copper fiber a suspended inside the hood portion was visually discolored after 2 hours, and after 6 hours, the whole turned black and lost its metallic luster (Fig. 6(B)).
  • the copper fiber b which was separated from the gas outlet by 15 cm, showed no discoloration and no loss of metallic luster even after 6 hours. This test also confirmed that the effect of metal corrosion was reduced when the gas outlet was spaced apart.
  • influenza virus inactivation test The present applicant discloses the results of an influenza virus inactivation test in the previous Patent Document 1. According to the test results, it was confirmed that the influenza virus can be deactivated simply by filling a space to be sterilized with a relative humidity of 30% to 50% with an extremely low concentration gas of 7 ppb. there is
  • hypochlorous acid gas concentration was further reduced, and a virus inactivation test was carried out.
  • the inside of the test container of 1.2 m 3 was adjusted to a relative humidity of 30% or 50%, and the gas was diffused to about 2 ppb. It was confirmed how the virus was inactivated by the presence or absence of
  • FIG. 7 shows the results of the influenza virus inactivation test.
  • FIG. 7(A) shows a logarithmic graph of changes in viral infectivity over time
  • FIG. 7(B) shows real values of viral infectivity at each measurement time point.
  • the virus was reduced faster at a humidity of 50% than at a humidity of 30%.
  • the initial value of the virus infectivity titer was about 68% immediately after the start of the experiment compared to when the relative humidity was 30%. It was confirmed that humidity plays a large role in suppressing the initial value of virus infectivity.
  • the environmental standard for chlorine gas in the air where people can live safely is 0.5 ppm. Since the environmental standard for hypochlorous acid gas has not been established, it was confirmed that the virus can be deactivated with a gas having a concentration of about 1/250 compared to the above environmental standard.
  • FIG. 8A shows changes in gas concentration
  • FIG. 8B shows changes in humidity and temperature in the test chamber.
  • line A indicates relative humidity
  • line B indicates temperature. It was confirmed that as the relative humidity increased, the gas concentration reached a peak, maintained a saturated state, and then decreased.
  • the initial relative humidity was 45%. Since the humidity at the start of the experiment was suitable for gas generation and was in a humidity region with a long half-life cycle, the gas increased steeply, reaching a maximum concentration of about 25 ppb at a relative humidity of about 60% 30 minutes after the start. became. As confirmed in the "first confirmation test of the correlation between the relative humidity and the amount of gas generated (hereinafter referred to as the first confirmation test)", the generation of gas slows down after the relative humidity exceeds 50%, Since the half-life period was also shortened, the gas concentration reached a saturated state with a peak of 25 ppb, which continued for about 10 minutes.
  • the generator 1 it is possible to generate a concentration of 2 ppb or more that is 10 times higher than the 2 ppb in which the deactivation of the virus has been confirmed in a room with an air volume of 25 m 3 and to control the gas concentration by the relative humidity of the space, which is safe and effective. It was confirmed that the virus could be inactivated in
  • Example 1 the generator 1 equipped with the moisture release amount suppressing means will be described with reference to FIG. FIG. 1(A) shows a vertical sectional view of the generator, and FIG. 1(B) shows a horizontal sectional view taken along the line AA in FIG. 1(A).
  • the generator 1 is a device having a hypochlorous acid gas generating structure.
  • the generator 1 consists of a main body 10, an inner lid 20 fitted above the main body, and an outer lid 30 having a gas discharge port 31 (see FIG. 1(A)).
  • the main body 10 includes a hypochlorous acid water storage tank 11, an outer cylindrical wall 12 forming a double cylindrical wall, an air pressurization means 13, a hypochlorous acid water misting means 14, and a gas
  • An inlet 15 and a gas path from the gas inlet to the inner lid are provided.
  • An inner cylindrical wall 21 is suspended from the inner cover 20 .
  • the outer cylindrical wall 12 forming a double cylindrical wall is attached to four spacers 16 dispersedly disposed on the bottom plate of the storage tank so that the inner cylindrical wall 21 and the mist generating means 14 are coaxially arranged. It is placed and positioned (see FIG. 1(B)).
  • the inner lid 20 includes an inner cylindrical wall 21 forming a double cylindrical wall, a gas passage for introducing outside air into the inner cylindrical wall 21, and a hanging wall 24 arranged in the gas passage downstream of the outer cylindrical wall 12. are provided (see FIG. 1(A)).
  • the length by which the inner cylindrical wall 21 hangs is set to a length that allows a gap 23 forming a gas path between the inner cylindrical wall 21 and the water surface of the hypochlorous acid water.
  • the inner cylindrical wall 21 suspended from the inner lid 20 and the outer cylindrical wall 12 erected from the reservoir 11 form a double cylindrical wall.
  • the outer lid 30 is placed on the inner lid 20, the inside of the inner cylindrical wall from the gas inlet 15, the gap 23 between the lower peripheral edge of the inner cylindrical wall and the hypochlorous acid water surface, and the double cylindrical wall A gas path is formed that reaches the gas discharge port 31 through the gap space 26 .
  • the gas discharge port 31 is opened in the top surface of the outer lid and positioned outside the area of the outer cylindrical wall 12 (see FIG. 1).
  • the air When air is pressurized and induced from the gas inlet 15 by the air pressurizing means 13, the air is introduced through the gas path formed in the inner lid 20 into the inner space of the inner cylindrical wall 21 that generates mist. Air mixed with mist descends along the space. The pressurized mist and the outside air are lowered, and flow uniformly from the peripheral gap 23 between the bottom of the inner cylindrical wall and the water surface to the gap space 26 between the inner and outer cylindrical walls, and the gap space Ascend 26. At this time, the mist formed into droplets in the clearance space 26 adheres to the wall surface between the inner cylindrical wall and the outer cylindrical wall and is dropped and collected in the storage tank 11 .
  • the gas-phase mist and gas rise to the upper portion of the outer cylindrical wall 12, head toward the opening 27 of the inner lid, and are introduced through the opening 27 into the space between the inner and outer lids, where they exit the gas discharge port. 31 and is released into the space to be sterilized. While the mist is guided through the gas path by the pressurized air, hypochlorous acid in a liquid phase is dropped into the storage tank 11, and only the hypochlorous acid in a gaseous state reaches the gas outlet, As in the moisture release test described above, the amount of moisture released into the space to be sterilized is suppressed (see Table 3).
  • the inner lid is provided with a hanging wall 24 that traverses the gas path, fine mist in a liquid state becomes droplets by the hanging wall 24 even outside the region of the outer cylindrical wall, and the storage tank 11 to be recovered. Although most of the mist in the liquid state is removed when it reaches the hanging wall 24, the provision of the hanging wall 24 can further suppress the amount of water generated.
  • the lower part of the storage tank 11 may be provided with a drive unit for the misting means 14 and as a storage place for the hypochlorous acid water tank 22 . Since the outer cylindrical wall 12 is placed on the spacer 16, and the hypochlorous acid water storage tank 11 is communicated between the inside and the outside of the outer cylindrical wall, drops that fall outside the outer cylindrical wall also enter the outer cylindrical wall. Droplets that have fallen are also collected in the storage tank 11 . Since the lower part of the outer cylindrical wall 12 is immersed in the reservoir 11, the disturbance of the water surface inside the outer cylindrical wall does not affect the area outside the outer cylindrical wall (Fig. 1A). (see diagram).
  • the outer cylindrical wall 12 and the side wall 17 of the inner lid 20 are separated by a gap 25 through which gas can flow (see FIG. 1(B)).
  • the hypochlorous acid mist guided from the gap space 26 between the double cylindrical walls to the side opposite to the gas discharge port 31 bypasses the gap 25 between the outer cylindrical wall 12 and the side wall 17 and is guided to the gas discharge port 31.
  • the height of the outer cylindrical wall 12 is such that when the inner lid 20 is fitted to the main body 10, the inner lid 20 and the outer cylindrical wall 12 are separated from each other to form a gas passage.
  • a fan corresponding to the pressure loss caused by the filter may be selected so that the gas can be released even when a filter is attached to the gas outlet 31.
  • the hypochlorous acid water misting means 14 is arranged coaxially with the double cylindrical wall, and is composed of a dispersing means 18, a cylindrical mesh body 19, and a driving part that rotates them integrally.
  • the diffusing means 18 is a funnel whose cross-sectional area decreases toward the bottom. The lower end opening of the funnel is immersed in the storage tank 11, the upper end is closed with a lid member, and the liquid droplets scatter around the upper peripheral edge.
  • the openings 28 are arranged radially.
  • a radially protruding brim 29 is provided at the upper end of the funnel, and a cylindrical mesh 19 hangs down from the outer edge of the brim 29 .
  • the mesh body 19 is made of stainless steel and has a mesh diameter of about 1 mm.
  • the dissipating means 18 and the mesh 19 are rotated integrally.
  • the hypochlorous acid water is pumped up along the inner surface of the funnel body forming the dissipating means, is dispersed as droplets from the dispersing port 28, and is rotated. 19 will collide.
  • hypochlorous acid mist Since the hypochlorous acid mist is generated in the inner cylindrical wall 21 by the droplets collided with the mesh 19 and crushed, the hypochlorous acid mist can be generated efficiently.
  • the hypochlorous acid water in the liquid phase state that did not become mist adheres to the wall surface of the inner cylindrical wall 21 due to the force of diffusion, drips down along the wall surface, and most of it falls into the storage tank 11 and is collected. be.
  • Example 2 the gas outlet 31 of the generator is fitted with a filter 40 serving as a means for suppressing the amount of water released, and the gas outlet is provided with a gas diffusion means 41.
  • the generator 2 is shown in FIGS. to explain.
  • FIG. 9(A) shows the configuration thereof
  • FIG. 9(B) shows an enlarged view of a non-woven fabric filter that constitutes the first moisture release suppressing means.
  • FIG. 9 in order to facilitate understanding, only the filter 40 and the gas diffusion means 41 are indicated by solid lines, and other configurations of the generator are indicated by broken lines.
  • FIG. 10 shows another aspect of the filter.
  • FIG. 10(A) shows a nanofilter 50 forming the second moisture release suppressing means
  • FIGS. shows a filter for FIG. 11(A) shows a photograph of the upstream surface of the non-woven fabric filter 40 in the embodiment of FIG. 9(A)
  • FIG. 11(B) shows a photograph of the upstream surface of the nanofilter 50 of FIG. 10(A). A magnified photo is shown.
  • the generator 2 may be fitted with any type of filter at the gas outlet depending on the performance of the air pressurizing means.
  • the filter When the filter is attached, the speed of gas discharge from the gas discharge port is reduced and the gas is retained near or at a low position. Therefore, a fan serving as a gas diffusion means is provided along the filter surface of the gas discharge port. , the gas is diffused in a short time over a wide range of the space to be sterilized.
  • the filter of either aspect By air-tightly attaching the filter of either aspect to the gas discharge port with a rubber packing 42 or the like, the gas passes only through the filter portion and is discharged into the sterilization target space.
  • the pressure inside the device increases, and hypochlorous acid may leak from the boundary between the main body, the inner lid, and the outer lid. should be airtight (see FIG. 9(A)).
  • the first water release amount suppressing means is a non-woven fabric filter that has undergone water-repellent treatment equivalent to that of a non-woven fabric mask worn by a person.
  • the fibers forming the filter have a fiber diameter of 1 ⁇ m or more and 6 ⁇ m or less and a pressure loss of about 30 Pa.
  • the non-woven fabric filter is not bent and is attached to the gas discharge port 31 in a flat state so that the hypochlorous acid mist does not leak.
  • a rubber packing 42 or the like may be provided around the filter and brought into close contact with the gas discharge port to ensure airtightness.
  • the material of the fiber forming the filter may be polypropylene resin fiber, polyester resin fiber, polyurethane resin fiber, or mixed resin fiber of these, but is not limited.
  • the manufacturing method of the non-woven fabric filter is not limited as long as it is water-repellent, and may be, for example, a meltblown manufacturing method, a spunbond manufacturing method, or the like.
  • the nonwoven fabric filter When the nonwoven fabric filter was attached to the generator and the generator was operated continuously for 6 hours, the entire upstream surface of the nonwoven fabric filter was wet (see Fig. 11 (A)). The downstream surface of the nonwoven fabric filter was not wet. As shown in the moisture release test, the amount of released water was suppressed, and gas was generated as shown in the gas generation test.
  • the pressure loss of the filter should be 20 Pa or more and 60 Pa or less, the fiber diameter of the filter should be 1 ⁇ m or more and 30 ⁇ m or less, and the mask need not necessarily be a non-woven fabric mask worn by people.
  • the second water release amount suppressing means is a hydrophobic nanofilter having a fiber diameter of 70 nm or more and 200 nm or less and a pressure loss of 20 Pa or more and less than 60 Pa.
  • the surface is bent once at the central portion so as to form a downwardly convex inclined surface (see FIG. 10(A)).
  • the nanofilter is a three-layer structure nanofilter 50 composed of a three-dimensional mesh layer 51 in which nanofibers are densely packed and thin nonwoven fabric layers 52 forming shape-retaining layers on both sides.
  • the mist that forms droplets on the upstream surface due to long-term continuous operation gathers in the center along the inclined surface and drops into the storage tank 11 to be collected.
  • the nanofilter was attached to the generator and it was operated continuously for 6 hours, the mist that did not pass through the upstream surface of the nanofilter adhered to the upstream surface of the nanofilter as fine droplets a, and the large droplets were dropped (Fig. 11).
  • B as shown in the moisture release test, the moisture release amount was suppressed. Note that the downstream surface was not wet.
  • the third moisture release suppressing means is a double filter composed of nonwoven fabric filters 61 and 62 and a nanofilter 50, and the space between the filters is A space 63 separated by 5 mm or more is provided.
  • the non-woven fabric filters 61 and 62 are inclined and attached to the frame so that the upstream surface is an inclined surface.
  • the entire nonwoven fabric filter may be inclined (see FIG. 10(B)). In this case, droplets adhering to the nonwoven fabric gather at the peripheral edge along the inclined surface and quickly drop.
  • Example 3 a building 5 in which an air conditioning system 4 having a hypochlorous acid gas generating structure is installed in the air conditioning path of each floor will be described with reference to FIG.
  • FIG. 12A shows an explanatory diagram explaining the configuration of the air conditioning system 4
  • FIG. 12B shows an explanatory diagram of the building 5.
  • the air conditioning system 4 is provided in an air conditioning path 80 that introduces outside air and distributes it to living rooms.
  • the air-conditioning system 4 in the range enclosed by the dashed line in FIG. 12(A) may be provided.
  • Chlorous acid water may be used, and hypochlorous acid water may be directly supplied.
  • the air conditioning system 4 introduces air by branching a part from the main air conditioning path 80, introduces the air pressurized by the air pressurizing means 13 into the inner cylindrical wall 21, and rotates in the inner cylindrical wall 21.
  • a fine hypochlorous acid mist is generated by a misting means 14 consisting of a cylindrical mesh body and hypochlorous acid water diffusion means, and the space in the inner cylindrical wall 21 is filled with the air and the mist. After the hypochlorous acid is lowered once, the hypochlorous acid in the gaseous state is raised in the gap space 26 between the inner cylindrical wall and the outer cylindrical wall 12 .
  • the gas outlet provided in the upper part outside the area of the outer cylindrical wall 12 where droplets do not occur from the water surface of the hypochlorous acid water storage tank 11.
  • mist of hypochlorous acid water and hypochlorous acid gas in gaseous state are supplied to the main air conditioning path 80. - ⁇
  • the hypochlorous acid gas supplied to the main air-conditioning route is combined with air whose temperature and humidity have been adjusted in advance, and is supplied to the living room.
  • Hypochlorous acid gas has a different half-life cycle depending on humidity. is preferably generated and supplied, but is not limited thereto.
  • the space where people stay in building 5 is divided into areas where hypochlorous acid gas with a concentration that can utilize the virus deactivation effect can be supplied according to the period of the half-life cycle according to the humidity, and air conditioning is performed.
  • the system 4 should be provided.
  • each floor is equipped with an air conditioning system 4 for easy understanding (see FIG. 12(B)).
  • an air conditioning system 4 for easy understanding (see FIG. 12(B)).
  • the air-conditioned area of one floor is large, it is preferable to equip one floor with a plurality of air-conditioning systems.
  • the air conditioning system 4 can be applied not only to large offices but also to buildings having many rooms for the elderly, and can provide building users with a comfortable and safe space.

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Abstract

This hypochlorous acid gas generation structure comprises a hypochlorous acid water storage tank and double cylindrical walls and is characterized in that a lower part of the outer cylindrical wall is immersed in hypochlorous acid water, a lower part of the inner cylindrical wall is separated from hypochlorous acid water, the hypochlorous acid water is made into mist within the inner cylindrical wall, the hypochlorous acid water in a liquid droplet state is dribbled down on the inner cylindrical wall and collected in the storage tank, the mist in a vapor phase state is evenly introduced into the space between the double cylindrical walls through the gap between the bottom of the inner cylindrical wall and the surface of the hypochlorous acid water in the storage tank, the mist in the vapor phase state attaches on the inner surfaces of the double cylindrical walls while the mist rises and becomes droplets, the droplets are collected, and only hypochlorous acid in the vapor phase state is discharged from a gas discharge port unaffected by airborne droplets from the hypochlorous acid water surface and is characterized by suppressing humidification of a space to be subjected to microorganism elimination and discharging only the hypochlorous acid gas in the vapor phase state that deactivates viruses.

Description

次亜塩素酸ガス発生構造、次亜塩素酸ガス発生装置、空調システムおよび建物Hypochlorous acid gas generating structure, hypochlorous acid gas generator, air conditioning system and building
 本発明は、除菌対象空間の加湿を抑えて、次亜塩素酸水からウイルスを失活させる気相状態の次亜塩素酸ガスだけを放出させ、除菌対象空間に短時間で均一に薄い濃度の次亜塩素酸ガスを供給することができる次亜塩素酸ガス発生構造、次亜塩素酸ガス発生装置、空調システムおよび建物に関する。 The present invention suppresses humidification of the space to be sterilized, releases only the hypochlorous acid gas in the gas phase that deactivates the virus from the hypochlorous acid water, and uniformly thins the space to be sterilized in a short time. The present invention relates to a hypochlorous acid gas generating structure, a hypochlorous acid gas generator, an air conditioning system and a building capable of supplying concentrated hypochlorous acid gas.
 具体的には、次亜塩素酸ガス発生装置は、下方に次亜塩素酸水の貯留槽を備え、外円筒壁と内円筒壁の二重の円筒壁を有し、外円筒壁の下方部を次亜塩素酸水に浸漬させ、内円筒壁の下方部を次亜塩素酸水から離間させ、内円筒壁の内部で次亜塩素酸水をミスト化させ、液滴状態の次亜塩素酸水は、内円筒壁に伝わせて貯留槽に回収し、気相状態となるミストは、内円筒壁の下方と貯留槽の次亜塩素酸水面との隙間を通して、二重の円筒壁の間の隙間空間を上昇させる。 Specifically, the hypochlorous acid gas generator is equipped with a hypochlorous acid water storage tank at the bottom, has a double cylindrical wall of an outer cylindrical wall and an inner cylindrical wall, and has a lower portion of the outer cylindrical wall is immersed in hypochlorous acid water, the lower part of the inner cylindrical wall is separated from the hypochlorous acid water, the hypochlorous acid water is misted inside the inner cylindrical wall, and hypochlorous acid in the form of droplets Water is transmitted to the inner cylindrical wall and collected in the storage tank, and the mist, which is in a gas phase state, passes through the gap between the bottom of the inner cylindrical wall and the hypochlorous acid water surface of the storage tank, and flows between the double cylindrical walls. Raise the gap space of
 そして、気相状態となるミストが上昇している間に、二重の円筒壁の内面に付着して滴となるミストを、下方の貯留槽に回収させ、気相状態となる次亜塩素酸のみを、次亜塩素酸水面からの飛沫の影響を受けないガス放出口から放出させる。健康被害と金属腐食が危惧されている液相状態の次亜塩素酸を放出させないで、気相状態の次亜塩素酸ガスだけを発生させる次亜塩素酸ガス発生構造、発生装置、空調システムおよび建物に関する。 Then, while the mist in the gas phase is rising, the mist that adheres to the inner surface of the double cylindrical wall and becomes droplets is collected in the lower storage tank, and the hypochlorous acid in the gas phase is collected. Only is released from the gas outlet that is not affected by droplets from the hypochlorous acid water surface. Hypochlorous acid gas generating structure, generator, air-conditioning system, and hypochlorous acid gas generating structure, generator, and air conditioning system that generate only gaseous hypochlorous acid gas without releasing liquid hypochlorous acid, which is feared to cause health hazards and metal corrosion. Regarding buildings.
 次亜塩素酸とは、水素原子と塩素原子と酸素原子とが結合されてなる分子で、常温常圧で液相状態または気相状態で存在する。本願では、次亜塩素酸が液体の水に溶解された状態を「次亜塩素酸水」と称し、次亜塩素酸が微細な液滴とされて空気中を浮遊している状態を「ミスト」と称し、気相状態の次亜塩素酸を「次亜塩素酸ガス」と称している。なお、大きさ5μm以下のミストは瞬間的に気化されるため、気相状態の次亜塩素酸ガスに含めている。 Hypochlorous acid is a molecule made up of hydrogen atoms, chlorine atoms, and oxygen atoms bonded together, and exists in either a liquid phase or a gas phase at normal temperature and pressure. In this application, the state in which hypochlorous acid is dissolved in liquid water is referred to as "hypochlorous acid water", and the state in which hypochlorous acid is suspended in the air as fine droplets is referred to as "mist ”, and hypochlorous acid in the gas phase state is called “hypochlorous acid gas”. Mist with a size of 5 μm or less is included in hypochlorous acid gas in a gaseous state because it is vaporized instantaneously.
 従来から、次亜塩素酸水から発生させたミストを生活空間に放出させ、浮遊ウイルスや付着ウイルスを失活させるとする多くの種類のウイルス失活装置が提供されている。新型コロナウイルス(COVID-19)のパンデミックにより、生活空間におけるウイルスの失活は喫緊の課題となり、コロナ禍以前に比べて次亜塩素酸を用いるウイルス失活装置が強い関心を集めることになった。 Conventionally, many types of virus deactivation devices have been provided that emit mist generated from hypochlorous acid water into living spaces to deactivate airborne viruses and adhering viruses. Due to the pandemic of the new coronavirus (COVID-19), virus deactivation in living spaces has become an urgent issue, and virus deactivation equipment using hypochlorous acid has attracted strong interest compared to before the corona disaster. .
 ところが、単なる加湿器で粒径の大きい次亜塩素酸のミストを放出させる装置が流通されたこと、スプレーで次亜塩素酸水を空間噴霧させたこと等によって、ミストを人が吸い込むことによる健康被害の発生が危惧された。WHO、厚生労働省等は、呼吸器に及ぼす健康被害を危惧して、次亜塩素酸水の空間噴霧を推奨しないとの見解を示した。特に、呼吸器疾患の持病のある者、成長過程にある幼児、児童等の健康被害が懸念され、次亜塩素酸を用いるウイルス失活装置の普及が停滞した。 However, due to the distribution of simple humidifiers that emit hypochlorous acid mist with large particle diameters, and the use of sprays that spray hypochlorous acid water in space, there has been an increase in the number of people who inhale the mist, resulting in health problems. It was feared that damage would occur. The WHO, the Ministry of Health, Labor and Welfare, etc. have expressed their view that they do not recommend spatial spraying of hypochlorous acid water due to concerns about health hazards on respiratory organs. In particular, the spread of virus inactivation devices using hypochlorous acid has been stagnant due to concerns about the health hazards of people with chronic respiratory diseases, growing infants and children.
 一方「一般社団法人 次亜塩素酸水普及促進会議」のホームページによれば、低濃度の次亜塩素酸水を空間噴霧した事例が開示されている。これによれば、海外を含めて多くの空間噴霧の事例があり、国内でも人の集まるイベント会場等での空間噴霧の実例が示され、目立った健康被害がないことが主張されている。 On the other hand, according to the website of the "General Incorporated Association Hypochlorous Acid Water Promotion Council", a case of spatial spraying of low-concentration hypochlorous acid water is disclosed. According to this, there are many cases of spatial spraying, including overseas, and examples of spatial spraying at event venues where people gather are shown in Japan, and it is claimed that there is no noticeable health hazard.
 特許文献1には、本出願人による、相対湿度30%から50%の低湿度においても、インフルエンザウイルスを失活させる装置の技術が開示されている。この技術は、真菌類の繁殖を抑制できる低い湿度において、次亜塩素酸ガスにより浮遊ウイルスを失活させるために、液滴・液体微粒子の発生による加湿を抑えている。 Patent Document 1 discloses a technology of a device that inactivates influenza viruses even at low humidity of 30% to 50% relative humidity by the present applicant. This technology suppresses humidification due to the generation of liquid droplets and liquid particles in order to deactivate airborne viruses with hypochlorous acid gas at low humidity that can suppress the growth of fungi.
 具体的には、液相状態のまま次亜塩素酸溶液を旋回揺動させて、空気循環部の空気と次亜塩素酸溶液との面摩擦により次亜塩素酸ガスを発生させ、空気取入口と空気放出口との気圧差により、空気を導入させると共に次亜塩素酸ガスを含んだ空気を放出させ、水分放出量を抑制させた状態で次亜塩素酸ガスを放出させる装置とされている。 Specifically, the hypochlorous acid solution is rotated and oscillated in a liquid state, and hypochlorous acid gas is generated by surface friction between the air in the air circulation unit and the hypochlorous acid solution, and the air intake is It is a device that introduces air and releases air containing hypochlorous acid gas due to the pressure difference between the air outlet and the air outlet, and releases hypochlorous acid gas while suppressing the amount of moisture released. .
 ところが、この装置によれば、次亜塩素酸水から液滴・液体微粒子を発生させないように、飛沫が飛ばない液相状態を保つ必要があり、次亜塩素酸水の旋回揺動を高速にできず、また装置の大型化も困難であるという課題があった。そのため、次亜塩素酸ガスの発生量が限られ、小さな空間でしかウイルスを失活できないことに加えて、空間全体に短時間で次亜塩素酸ガスを放散することができないという課題があった。 However, according to this device, it is necessary to maintain a liquid phase state where droplets do not fly so that the hypochlorous acid water does not generate droplets or liquid fine particles. In addition, there is a problem that it is difficult to increase the size of the apparatus. For this reason, the amount of hypochlorous acid gas generated is limited, and in addition to being able to inactivate the virus only in a small space, there was a problem that hypochlorous acid gas could not be diffused throughout the entire space in a short time. .
 本発明者は、この装置の開発後、次亜塩素酸ガスが活性を維持する活性有効期間を確認するために、空間の相対湿度と次亜塩素酸ガスの半減周期との関係を確認試験した。また相対湿度に応じた次亜塩素酸ガスのウイルス失活効果を確認試験した。これらの試験結果から、相対湿度を60%以下に抑制させておくと、次亜塩素酸水から次亜塩素酸ガスが効果的に発生されるだけでなく、揮発させた次亜塩素酸ガスの活性を維持させやすいことを発見した。 After the development of this device, the present inventor conducted a test to confirm the relationship between the relative humidity of the space and the half-life period of hypochlorous acid gas in order to confirm the active period during which hypochlorous acid gas maintains its activity. . In addition, we confirmed the virus inactivation effect of hypochlorous acid gas according to the relative humidity. From these test results, if the relative humidity is suppressed to 60% or less, not only hypochlorous acid gas is effectively generated from hypochlorous acid water, but also the volatilized hypochlorous acid gas It was found that it was easy to maintain the activity.
 特許文献2には、水および空気が通過可能な回転する円筒状の網体を設け、この網体の内壁に水を衝突させて水をミスト化し、水の表面積を増大させ、処理室内を通過する被処理空気のマイナスイオンの濃度を増大させるとするマイナスイオン発生装置の技術が開示されている。 In Patent Document 2, a rotating cylindrical net body through which water and air can pass is provided, and the water collides with the inner wall of the net body to turn the water into mist, thereby increasing the surface area of the water and allowing it to pass through the processing chamber. There is disclosed a technology of a negative ion generator for increasing the concentration of negative ions in the air to be treated.
 この技術に開示された装置によれば、網体を回転させて水をミスト化させている空間の上方から水面に向けて空気を噴き付けさせ、網体によるミストを含んだ空気を水面に衝突させ、上方に反転させて放出口から空気を排出させている。この技術によれば、噴き付けられた空気によって、水面が攪乱され、水面からの飛沫が多く発生し、網体によりミスト化された空気と共に飛沫による粒径の大きなミストも外気に放出され、空間の湿度が高くなりやすいという課題があった。 According to the device disclosed in this technique, the net body is rotated to blow air from above the space in which the water is turned into mist, toward the water surface, and the mist-laden air from the net body collides with the water surface. and is turned upside down to discharge the air from the discharge port. According to this technology, the water surface is disturbed by the blown air, and many droplets are generated from the water surface. There was a problem that the humidity of the air tends to be high.
 特許文献3には、マイナスイオン発生装置の装置本体を小型化させるとする技術が開示されている。この技術によれば、筒状体とされたケースの中に同心状に内筒を配し、ケースと内筒の下方部を水没させて、内筒の一部に切欠き部を設けて内筒からケースへの通気部とし、内筒内で発生させた水ミスト混合空気を、前記切欠き部からケースと内筒の間に通して、旋回運動させ上昇させて外部に放出させるとしている。 Patent Document 3 discloses a technique for miniaturizing the main body of a negative ion generator. According to this technique, an inner cylinder is arranged concentrically in a cylindrical case, the case and the lower part of the inner cylinder are submerged, and a notch is provided in a part of the inner cylinder to form an inner cylinder. Air mixed with water mist generated in the inner cylinder is passed through the notch between the case and the inner cylinder through the notch, raised by a swirling motion, and released to the outside.
 しかしこの技術によれば、内筒の中の水面は下降流の衝突により、また、ケースと内筒との間の水面は切欠きを通して発生される旋回流により攪乱され、いずれの水面からも多くの飛沫が発生され、仮に水滴が落下回収されたとしても、マイナスイオンとともに多湿の空気が発生されるという課題があった。 However, according to this technique, the water surface in the inner cylinder is disturbed by the collision of the downward flow, and the water surface between the case and the inner cylinder is disturbed by the swirling flow generated through the notch, and many is generated, and even if the water droplets are dropped and collected, there is a problem that humid air is generated together with negative ions.
 特許文献2および特許文献3に記載の技術に次亜塩素酸水を適用させたときには、除菌対象空間の相対湿度を次亜塩素酸ガスの放散には適さない60%以上まで加湿させると共に、液相状態の次亜塩素酸ミストも除菌対象空間に放散させる可能性があった。そこで本出願人は、液滴・液体微粒子の液相状態の次亜塩素酸水を発生させないで、次亜塩素酸ガスだけを発生させると共に、放出させた除菌空間の湿度をあげにくい技術の開発に鋭意務め、本願発明に想到した。 When hypochlorous acid water is applied to the techniques described in Patent Documents 2 and 3, the relative humidity of the space to be sterilized is humidified to 60% or more, which is not suitable for the diffusion of hypochlorous acid gas. Hypochlorous acid mist in a liquid state could also diffuse into the space to be sterilized. Therefore, the applicant has developed a technology that generates only hypochlorous acid gas without generating hypochlorous acid water in the liquid phase state of droplets and liquid particles, and makes it difficult to increase the humidity of the released sterilization space. He devoted himself to the development and conceived of the present invention.
特許文献1:国際公開2021-49045号公報
特許文献2:特開平9-203540号公報
特許文献3:特開平9-264574号公報
Patent Document 1: International Publication No. 2021-49045 Patent Document 2: JP-A-9-203540 Patent Document 3: JP-A-9-264574
 本発明が解決しようとする課題は、除菌対象空間の加湿を抑えて、次亜塩素酸水からウイルスを失活させる気相状態の次亜塩素酸ガスだけを放出させ、対象空間に短時間で均一に薄い濃度の次亜塩素酸ガスを供給することができる次亜塩素酸ガス発生構造、次亜塩素酸ガス発生装置、空調システムおよび建物を提供することである。 The problem to be solved by the present invention is to suppress humidification of the space to be sterilized, release only the hypochlorous acid gas in the gaseous state that deactivates the virus from the hypochlorous acid water, and allow the space to be disinfected for a short time. To provide a hypochlorous acid gas generating structure, a hypochlorous acid gas generator, an air-conditioning system and a building capable of supplying hypochlorous acid gas having a uniformly low concentration.
 本発明の第1の発明は、気相状態の次亜塩素酸のみを発生させる次亜塩素酸ガス発生構造において、前記次亜塩素酸ガス発生構造が、次亜塩素酸水の貯留槽と、二重の円筒壁と、気体経路と、空気加圧手段と、次亜塩素酸水のミスト化手段と、ガス放出口とを含み、二重の円筒壁をなす外円筒壁が、前記貯留槽から起立されると共に下方部が次亜塩素酸水に浸漬され、二重の円筒壁をなす内円筒壁が、その下方周囲と前記貯留槽の次亜塩素酸水面との間に隙間を備えるように垂下されて、内円筒壁の内部を気体経路となし、前記貯留槽が、前記外円筒壁の内外に貫通され、前記空気加圧手段が、気体導入口から、内円筒壁の内部を通してガス放出口まで外気を加圧誘導させ、前記ミスト化手段が、円筒状の網体と、次亜塩素酸水の放散手段を備え、前記網体が、二重の円筒壁と同心をなして回転され、前記放散手段が、前記内円筒壁の内部で前記網体に、次亜塩素酸水を衝突させてミストを発生させ、液相状態の次亜塩素酸水が、前記内円筒壁の内部で前記貯留槽に落下回収され、気相状態となる前記ミストが、前記隙間の周囲から前記二重の円筒壁がなす隙間空間に誘導されて上昇し、前記ミストが上昇している間に、前記隙間空間において滴となったミストが、前記隙間空間の領域で前記貯留槽に落下回収され、前記ガス放出口が、前記外円筒壁の領域外の上部に備えられ、前記ガス放出口から、気相状態となるミストと次亜塩素酸ガスのみが放出されることを特徴としている。 A first invention of the present invention is a hypochlorous acid gas generating structure for generating only hypochlorous acid in a gaseous state, wherein the hypochlorous acid gas generating structure comprises a storage tank of hypochlorous acid water, An outer cylindrical wall forming a double cylindrical wall includes a double cylindrical wall, a gas passage, an air pressurizing means, a hypochlorous acid water misting means, and a gas discharge port, and the storage tank and the lower part is immersed in the hypochlorous acid water, and the inner cylindrical wall forming a double cylindrical wall has a gap between the lower periphery and the hypochlorous acid water surface of the storage tank. and the inside of the inner cylindrical wall serves as a gas path, the storage tank penetrates the inside and outside of the outer cylindrical wall, and the air pressurizing means passes the gas from the gas inlet through the inside of the inner cylindrical wall. The outside air is pressurized and guided to the discharge port, the misting means comprises a cylindrical mesh body and hypochlorous acid water diffusion means, and the mesh body rotates concentrically with the double cylindrical wall. The diffusion means causes the hypochlorous acid water to collide with the net body inside the inner cylindrical wall to generate mist, and the hypochlorous acid water in a liquid phase is emitted inside the inner cylindrical wall. The mist that is dropped and collected in the storage tank and becomes a gas phase is guided upward from the periphery of the gap to the gap space formed by the double cylindrical walls, and while the mist is rising, The mist formed into droplets in the gap space is dropped and collected in the storage tank in the area of the gap space, and the gas discharge port is provided at an upper portion outside the region of the outer cylindrical wall, and from the gas discharge port, It is characterized by releasing only mist in gas phase and hypochlorous acid gas.
 次亜塩素酸水は、ジクロロイソシアヌル酸ナトリウムを水に溶解させてもよく、塩化ナトリウム水溶液を電気分解させて微酸性の次亜塩素酸水を生成させてもよく、製法は限定されない。次亜塩素酸水は、pHにより性状が異なるが、ウイルス失活効果に優れた次亜塩素酸ガスが発生されやすいpH3.0からpH7.5が好適である。 The hypochlorous acid water may be produced by dissolving sodium dichloroisocyanurate in water, or by electrolyzing an aqueous sodium chloride solution to generate slightly acidic hypochlorous acid water, and the manufacturing method is not limited. Hypochlorous acid water has different properties depending on the pH, but pH 3.0 to pH 7.5 is suitable because hypochlorous acid gas with excellent virus deactivation effect is easily generated.
 次亜塩素酸水のミスト化手段は、円筒状の網体と次亜塩素酸水の放散手段とされる。放散手段は下端が開放された漏斗状の回転体を次亜塩素酸水に浸漬させ、遠心力により次亜塩素酸水をくみ上げて、液滴として放散させてもよく、噴付手段により噴き付けさせてもよい。網体は、腐食が抑制されるようにステンレス製が好適であるが、網体の規格は限定されない。 The hypochlorous acid water misting means is a cylindrical mesh and hypochlorous acid water diffusion means. The dispersing means may immerse a funnel-shaped rotating body with an open bottom end in hypochlorous acid water, draw up the hypochlorous acid water by centrifugal force, and disperse it as droplets, and spray it by a spraying means. You may let The net body is preferably made of stainless steel so as to suppress corrosion, but the standard of the net body is not limited.
 放散手段により放散させた液滴を回転される網体に衝突させるため、内円筒壁の中に微細なミストを発生させることができる。空気加圧手段により、外気導入口から導入された空気は、ミストが発生されている内円筒壁の中の次亜塩素酸水面に向かって下降される。導入された空気と発生されたミストは、内円筒壁の下方と次亜塩素酸水面との周囲の隙間を通って、外円筒壁と内円筒壁との隙間空間に均等に導入されて上昇される。隙間の一部に片寄らず、隙間の周囲全体を均等に上昇されるため、外円筒壁の外の次亜塩素酸水面が撹乱されない。 Since the droplets dispersed by the dispersion means collide with the rotating mesh, fine mist can be generated inside the inner cylindrical wall. By the air pressurization means, the air introduced from the outside air inlet is lowered toward the surface of the hypochlorous acid water in the inner cylindrical wall where the mist is generated. The introduced air and the generated mist pass through the gap around the bottom of the inner cylindrical wall and the hypochlorous acid water surface, and are evenly introduced into the gap space between the outer cylindrical wall and the inner cylindrical wall and rise. be. Since the hypochlorous acid water surface outside the outer cylindrical wall is not disturbed because the entire circumference of the gap is raised evenly without being biased to a part of the gap.
 微細な径にならなかったミストは水滴状になり、内壁に沿って貯留槽に落下され回収される。微細な径になったミストは、内円筒壁と外円筒壁との隙間全体を均等に上昇するが、その過程でも滴となるミストもある。滴となったミストは、隙間に面した内円筒壁と外円筒壁の内面に付着し、貯留槽に落下して回収される。ガス放出口が、外円筒壁の領域外の上部に備えられているため、次亜塩素酸水面の攪乱による飛沫の影響を受けず、微細なミストのみがガス放出口に至る。 The mist that did not become fine diameter becomes droplets and falls along the inner wall into the reservoir and is collected. The fine mist rises evenly through the entire gap between the inner cylindrical wall and the outer cylindrical wall, but some of the mist becomes droplets in the process. The droplets of mist adhere to the inner surfaces of the inner cylindrical wall and the outer cylindrical wall facing the gap, drop into a storage tank, and are collected. Since the gas discharge port is provided in the upper portion outside the region of the outer cylindrical wall, only fine mist reaches the gas discharge port without being affected by droplets caused by disturbance of the hypochlorous acid water surface.
 次亜塩素酸ガスとともに、滴とならなかった微細なミストは、ガス放出口に至り、除菌対象空間に放出される。滴とならなかったミストは5μm以下の大きさであれば、瞬間的にガス化されるため、ガス放出口から放出されるときには次亜塩素酸ガスとなっている。なお、「気相状態となるミストと次亜塩素酸ガスのみ」とは、液相状態のままで放出される次亜塩素酸が含まれていなければよく、外気が含まれているのは勿論のことである。 Along with the hypochlorous acid gas, fine mist that did not form droplets reaches the gas outlet and is released into the space to be sterilized. If the size of the mist that does not form droplets is 5 μm or less, it is instantaneously gasified, so that when it is discharged from the gas discharge port, it becomes hypochlorous acid gas. In addition, "only mist and hypochlorous acid gas in gas phase" means that it does not need to contain hypochlorous acid that is released in liquid phase, and of course the outside air is included. It's about.
 本発明の第1の発明によれば、次亜塩素酸水をミスト化させて、内円筒壁の中でも、内円筒壁と外円筒壁の隙間の空間でも、液相状態となるミストを回収させて、気相状態となる微細なミストと次亜塩素酸ガスだけを、飛沫の影響を受けない外円筒壁の領域外に設けられたガス放出口から、ウイルスを失活させる除菌対象空間に放出させている。第1の発明によれば、加湿効果を抑制させた状態で、次亜塩素酸ガスだけを従来よりも多く放出させることができる。これにより、大きな空間に対しても、ウイルスを失活させる次亜塩素酸ガスを効果的に、短時間で発生させることができるという従来にない有利な効果を奏する。 According to the first aspect of the present invention, the hypochlorous acid water is turned into mist, and the mist in the liquid state is recovered in the inner cylindrical wall and in the space between the inner cylindrical wall and the outer cylindrical wall. Then, only fine mist and hypochlorous acid gas, which are in a gaseous state, are discharged from the gas outlet provided outside the area of the outer cylindrical wall, which is not affected by droplets, into the space to be disinfected to deactivate the virus. I am releasing it. According to the first invention, only hypochlorous acid gas can be released in a larger amount than before while suppressing the humidification effect. As a result, even in a large space, it is possible to effectively generate hypochlorous acid gas that deactivates viruses in a short period of time.
 本発明の第2の発明は、次亜塩素酸ガス発生装置において、気相状態の次亜塩素酸のみを発生させる次亜塩素酸ガス発生装置であって、第1の発明の次亜塩素酸ガス発生構造を備えていることを特徴としている。第2の発明によれば、第1の発明の次亜塩素酸ガス発生構造が一体の装置の中に構成されているため、簡易に移動して使用できるという効果を奏する。 A second invention of the present invention is a hypochlorous acid gas generator that generates only hypochlorous acid in a gas phase state, wherein the hypochlorous acid of the first invention It is characterized by having a gas generating structure. According to the second invention, since the hypochlorous acid gas generating structure of the first invention is configured in an integrated device, there is an effect that it can be easily moved and used.
 本発明の第3の発明は、第2の発明の次亜塩素酸ガス発生装置であって、前記ガス放出口には、第1の水分放出量抑制手段が装着可能とされると共に、前記気体経路の気体導入口から前記ガス放出口までが気密とされ、第1の水分放出量抑制手段が、繊維径が1μm以上30μm以下であると共に圧力損失が20Pa以上60Pa以下である撥水性を有する不織布フィルタとされていることを特徴としている。 A third invention of the present invention is the hypochlorous acid gas generator of the second invention, wherein the gas discharge port can be equipped with a first moisture release amount suppressing means, and the gas A water-repellent nonwoven fabric in which the path from the gas inlet to the gas outlet is airtight, and the first water release suppressing means has a fiber diameter of 1 μm or more and 30 μm or less and a pressure loss of 20 Pa or more and 60 Pa or less. It is characterized by being used as a filter.
 「気体経路の気体導入口から前記ガス放出口までが気密」とは、装置の本体と蓋との間の隙間等から液相状態のミストが漏れないように気密にされていることをいう。不織布フィルタは、ガス放出口の内外いずれに装着されてもよいが、内側に装着されると、ガスにならなかったミストが微細な水滴となり、貯水槽に落下されやすいため好適である。 "Airtight from the gas inlet of the gas path to the gas outlet" means that the gap between the main body and the lid of the device is airtight so that the mist in the liquid state does not leak. The non-woven fabric filter may be attached either inside or outside the gas discharge port, but if it is attached inside, the mist that did not turn into gas becomes fine water droplets and easily falls into the water tank, which is preferable.
 2021年に制定された日本産業規格「JIS T9001(医療用および一般用マスクの性能要件および試験方法)」によれば、人が着用するマスクの圧力損失が20Pa以上60Pa未満であることが規定された。第2の発明の不織布フィルタは、撥水性を有し、繊維径が1μm以上30μm以下であり、前記JIS規格を充足する圧力損失である入手容易なフィルタとしている。 According to the Japanese Industrial Standard "JIS T9001 (Performance requirements and test methods for medical and general masks)" established in 2021, the pressure loss of masks worn by people is specified to be 20 Pa or more and less than 60 Pa. rice field. The non-woven fabric filter of the second invention has water repellency, has a fiber diameter of 1 μm or more and 30 μm or less, and is an easily available filter that satisfies the JIS standard.
 また、一般用マスクに使用されるポリウレタン樹脂、ポリエチレン樹脂、ポリプロピレン樹脂等からなり静電処理された不織布フィルタであれば、圧力損失が約30Paであり、その撥水性と繊維径とにより、粒径が2μmまでのミストであれば98%以上の割合で除去させることができ好適である。第3の発明によれば、水分放出量を更に抑制させた状態で、次亜塩素酸ガスだけを効率よく放出させることができる。 In addition, an electrostatically treated non-woven fabric filter made of polyurethane resin, polyethylene resin, polypropylene resin, etc. used for general masks has a pressure loss of about 30 Pa, and depending on the water repellency and fiber diameter, the particle size If the mist is up to 2 μm, it can be removed at a rate of 98% or more, which is preferable. According to the third invention, only the hypochlorous acid gas can be efficiently released while the amount of water released is further suppressed.
 本発明の第4の発明は、第2の発明の次亜塩素酸ガス発生装置であって、前記ガス放出口には、第2の水分放出量抑制手段が装着可能とされると共に、前記気体経路の気体導入口から前記ガス放出口までが気密とされ、第2の水分放出量抑制手段が、繊維径が70nm以上200nm以下の疎水性ナノファイバーを含むと共に圧力損失が20Pa以上60Pa以下のナノフィルタとされていることを特徴としている。 A fourth invention of the present invention is the hypochlorous acid gas generator of the second invention, wherein the gas discharge port can be equipped with a second moisture release amount suppressing means, and the gas The path from the gas introduction port to the gas discharge port is airtight, and the second moisture release suppressing means includes hydrophobic nanofibers having a fiber diameter of 70 nm or more and 200 nm or less and a pressure loss of 20 Pa or more and 60 Pa or less. It is characterized by being used as a filter.
 第4の発明によれば、ガス放出口に第2の水分放出量抑制手段をなすナノフィルタが備えられる。繊維径が70nm以上200nm以下の疎水性ナノファイバーは、ファンデルワールス力により微細粒子を吸着ろ過させる。そのため、不織布フィルタでは除去できない大きさの物質、例えば粒径が100nmといった微細な水分、塩化物等の固形粒子さえも除去させることができる。 According to the fourth invention, the gas outlet is provided with a nanofilter that serves as the second means for suppressing the amount of water released. Hydrophobic nanofibers with a fiber diameter of 70 nm or more and 200 nm or less absorb and filter fine particles by Van der Waals force. Therefore, even substances of a size that cannot be removed by a non-woven fabric filter, for example, fine water particles with a particle diameter of 100 nm, and even solid particles such as chlorides can be removed.
 ファンデルワールス力は、静電処理とは異なり、繊維が濡れても、ろ過性能が低下されにくいため、次亜塩素酸ガス発生装置を長時間に亘って連続運転させる場合に、ナノファイバーを含んでいると好適である。ナノフィルタはナノファイバーのみからなる場合に限定されず、ナノファイバーの両面に形状保持層をなす不織布を備えさせてもよい。 Unlike electrostatic treatment, the van der Waals force does not reduce filtration performance even if the fibers get wet. It is preferable to be The nanofilter is not limited to being composed only of nanofibers, and may be provided with nonwoven fabric forming a shape-retaining layer on both sides of the nanofibers.
 また、ナノフィルタは単独で使用されてもよいが、第3の発明の不織布フィルタと二重にして使用されてもよい。疎水性ナノファイバーの材質は、例えばポリウレタン樹脂、ポリプロピレン樹脂等が繊維径を細くしやすく、好適である。第4の発明によれば、塩化物等の固形粒子さえも除去させることができると共に、水分放出量を更に抑制させることができ、次亜塩素酸ガス発生装置から気相状態のガスだけを放出させることができる。 In addition, the nanofilter may be used alone, or may be used in combination with the nonwoven fabric filter of the third invention. Suitable materials for the hydrophobic nanofibers include, for example, polyurethane resins and polypropylene resins, since the diameter of the fibers can be easily reduced. According to the fourth invention, even solid particles such as chlorides can be removed, and the amount of moisture released can be further suppressed, and only gas in the gas phase is released from the hypochlorous acid gas generator. can be made
 本発明の第5の発明は、第2の発明の次亜塩素酸ガス発生装置であって、前記ガス放出口には、第3の水分放出量抑制手段が装着可能とされると共に、前記気体経路の気体導入口から前記ガス放出口までが気密とされ、第3の水分放出量抑制手段が、上流側から、繊維径が1μm以上30μm以下であると共に圧力損失が20Pa以上60Pa以下である撥水性を有する不織布フィルタと、繊維径が70nm以上200nm以下の疎水性ナノファイバーを含むと共に圧力損失が20Pa以上60Pa以下のナノフィルタからなる二重のフィルタとされ、二重のフィルタの間が少なくとも5mm以上離間されていることを特徴としている。 A fifth invention of the present invention is the hypochlorous acid gas generator of the second invention, wherein the gas discharge port can be equipped with a third moisture release amount suppressing means, and the gas The path from the gas inlet to the gas outlet is airtight, and the third moisture release suppressing means is a repellent fiber having a fiber diameter of 1 μm or more and 30 μm or less and a pressure loss of 20 Pa or more and 60 Pa or less from the upstream side. A double filter consisting of a nonwoven fabric filter having water and a nanofilter containing hydrophobic nanofibers having a fiber diameter of 70 nm or more and 200 nm or less and having a pressure loss of 20 Pa or more and 60 Pa or less, and the distance between the double filters is at least 5 mm. or more.
 第5の発明によれば、ガス放出口に第3の水分放出量抑制手段をなす二重のフィルタが備えられる。二重のフィルタをなす不織布フィルタは第3の発明の不織布フィルタと同様であり、ナノフィルタは第4の発明のナノフィルタと同様である。 According to the fifth invention, the gas discharge port is provided with a double filter that serves as the third means for suppressing the amount of water released. The nonwoven fabric filter forming a double filter is the same as the nonwoven fabric filter of the third invention, and the nanofilter is the same as the nanofilter of the fourth invention.
 フィルタを二重にしても圧力損失が最大120Pa未満であり、HEPAフィルタの圧力損失の約2分の1であるため、大容量の装置にも適用可能である。圧力損失が小さいフィルタを組み合わせれば、通気性が高く、家庭用のガス発生装置に使用される通常のファンであっても、二重のフィルタを通してガスを放出させることができる。 Even if the filter is doubled, the maximum pressure loss is less than 120 Pa, which is about half the pressure loss of a HEPA filter, so it can be applied to large-capacity equipment. If a filter with low pressure loss is combined, gas can be discharged through a double filter even with a fan that has high air permeability and is used in a domestic gas generator.
 二重のフィルタが、少なくとも5mm以上離間されて配されるため、仮に、空気加圧手段の圧力により不織布フィルタの上流面に付着した微細水分が、二重のフィルタの間に噴き出すことがあっても、ナノフィルタに至るまでに微細水分が気化される。第5の発明によれば、ナノフィルタの隙間をミストにより詰まらせにくく、ガス発生装置を長時間に亘って連続運転させても、水分放出量を抑制させることができる。 Since the double filters are spaced apart by at least 5 mm, even if fine water adhering to the upstream surface of the non-woven fabric filter due to the pressure of the air pressurizing means, it may blow out between the double filters. Also, fine moisture is vaporized before reaching the nanofilter. According to the fifth invention, it is difficult for mist to clog the gaps of the nanofilter, and even if the gas generator is operated continuously for a long period of time, the amount of released water can be suppressed.
 本発明の第6の発明は、第3から第5の発明の次亜塩素酸ガス発生装置であって、前記ガス放出口に装着された前記水分放出量抑制手段の上流面が、傾斜面をなし、前記上流面で滴となったミストが、前記傾斜面に沿って前記貯留槽に落下されることを特徴としている。水分放出量抑制手段をなすフィルタが装着されると、フィルタの上流面が加圧され、装置を長時間に亘って連続運転させる間に、微細なフィルタを通過できなかったミストが、フィルタ表面に微細な水滴となり付着されることがある。 A sixth invention of the present invention is the hypochlorous acid gas generator according to the third to fifth inventions, wherein the upstream surface of the water release amount suppressing means attached to the gas discharge port is an inclined surface. None, the mist droplets on the upstream surface are dropped into the storage tank along the inclined surface. When the filter serving as the water release amount suppressing means is attached, the upstream surface of the filter is pressurized, and during long-term continuous operation of the apparatus, the mist that has not passed through the fine filter is deposited on the surface of the filter. It may become fine water droplets and adhere.
 第6の発明によれば、水分放出量抑制手段の上流面が、傾斜面をなしているため、微細な水滴を大きな水滴とさせやすく、傾斜面に沿って自然落下させやすい。水分放出量抑制手段が二重のフィルタの場合には、上流側すなわち貯留槽側に配される不織布フィルタだけの上流面を屈曲させるようにすると好適である。第6の発明によれば、次亜塩素酸ガス発生装置が、長時間に亘って連続運転されても、ガス発生量の低下がされにくく、安定してガスを放出させ続けることができる。 According to the sixth aspect of the invention, since the upstream surface of the water release amount suppressing means forms an inclined surface, fine water droplets are easily turned into large droplets and are easily allowed to naturally fall along the inclined surface. In the case where the moisture release amount suppressing means is a double filter, it is preferable to bend the upstream surface of only the non-woven fabric filter disposed on the upstream side, that is, on the storage tank side. According to the sixth invention, even if the hypochlorous acid gas generator is continuously operated for a long period of time, the amount of gas generated is unlikely to decrease, and the gas can be stably and continuously discharged.
 本発明の第7の発明は、第3から第5の発明の次亜塩素酸ガス発生装置であって、前記ガス放出口の外方に、気流を発生させるガス拡散手段が備えられ、前記ガス拡散手段が、前記ガス放出口から放出された次亜塩素酸ガスを拡散させることを特徴としている。 A seventh invention of the present invention is the hypochlorous acid gas generator according to the third to fifth inventions, wherein gas diffusion means for generating an air flow is provided outside the gas discharge port, and the gas is The diffusing means is characterized by diffusing the hypochlorous acid gas released from the gas outlet.
 フィルタにより次亜塩素酸ガスが放出されにくくなると、次亜塩素酸ガスが放出口近くに滞留されやすくなる。第7の発明によれば、ファンにより次亜塩素酸ガスを拡散させていることにより、半減周期の短い次亜塩素酸ガスをすみやかに拡散させることができ、高い濃度の次亜塩素酸ガスを片寄らせないで、気積の大きい部屋の隅々にまで薄い濃度の次亜塩素酸ガスを拡散させ、短時間でウイルスを不活化させると共に金属腐食を発生させにくい。 When the filter makes it difficult for hypochlorous acid gas to be released, it tends to accumulate near the release port. According to the seventh invention, by diffusing the hypochlorous acid gas with the fan, the hypochlorous acid gas having a short half-life period can be rapidly diffused, and the hypochlorous acid gas of high concentration can be diffused. It diffuses hypochlorous acid gas at a low concentration to every corner of a room with a large air volume, inactivating viruses in a short time and preventing metal corrosion.
 本発明の第8の発明は、空調システムにおいて、気相状態の次亜塩素酸のみを発生させて室内に供給させる空調システムであって、第1の発明の次亜塩素酸ガス発生構造を空調経路に備え、気相状態となるミストと次亜塩素酸ガスのみを、室内への新鮮空気導入経路に導入させて供給することを特徴としている。 An eighth invention of the present invention is an air conditioning system that generates only hypochlorous acid in a gaseous state and supplies it to a room in an air conditioning system, wherein the hypochlorous acid gas generating structure of the first invention is used for air conditioning. In preparation for the route, only mist and hypochlorous acid gas in a vapor phase state are introduced into the fresh air introduction route into the room and supplied.
 空調システムは、外部からの取り入れた空気を空気加圧手段により加圧して、新鮮空気供給経路に導入させればよい。第8の発明によれば、低い湿度環境とし、新鮮な外気による換気と共に次亜塩素酸ガスを供給し、真菌類の発生を抑えた状態で消臭、除菌等が行われ、高齢者や医療対象室に適した空調システムとすることができるという従来にない有利な効果を奏する。 The air conditioning system should pressurize the air taken in from the outside with the air pressurization means and introduce it into the fresh air supply path. According to the eighth invention, a low humidity environment is provided, hypochlorous acid gas is supplied together with ventilation with fresh outside air, and deodorization and sterilization are performed in a state where the growth of fungi is suppressed, and the elderly and An unprecedented advantageous effect can be obtained that an air-conditioning system suitable for a medical care room can be provided.
 本発明の第9の発明は、空調域が複数の区画に分割された建物において、人が滞在する区画毎に、気相状態の次亜塩素酸のみを発生させる第8の発明の空調システムが備えられていることを特徴としている。第9の発明によれば、空調域を複数の区画に分割させているため、ウイルス不活化作用を有する反面、半減周期が限られている次亜塩素酸ガスが、各区画に有効に供給される建物とすることができるという効果を奏する。 A ninth aspect of the present invention is a building in which the air-conditioned area is divided into a plurality of compartments. It is characterized by having According to the ninth invention, since the air-conditioned area is divided into a plurality of compartments, hypochlorous acid gas, which has a virus-inactivating effect but has a limited half-life cycle, is effectively supplied to each compartment. There is an effect that it can be a building that
・本発明の第1の発明によれば、加湿効果を抑制させた状態で、次亜塩素酸ガスだけを従来よりも多く放出させることができ、大きな空間に対しても、ウイルスを失活させる次亜塩素酸ガスを効果的に、短時間で発生させることができるという従来にない有利な効果を奏する。
・本発明の第2の発明によれば、第1の発明の次亜塩素酸ガス発生構造が一体の装置の中に構成されているため、簡易に移動して使用できるという効果を奏する。
・本発明の第3の発明によれば、水分放出量を更に抑制させた状態で、次亜塩素酸ガスだけを効率よく放出させることができる。
・According to the first aspect of the present invention, only hypochlorous acid gas can be released more than before while suppressing the humidification effect, and viruses can be deactivated even in a large space. An unprecedented advantageous effect of being able to generate hypochlorous acid gas effectively in a short period of time is exhibited.
- According to the second invention of the present invention, since the hypochlorous acid gas generating structure of the first invention is configured in an integrated device, there is an effect that it can be easily moved and used.
- According to the third aspect of the present invention, only hypochlorous acid gas can be efficiently released while the amount of water released is further suppressed.
・本発明の第4の発明によれば、塩化物等の固形粒子さえも除去させることができると共に、水分放出量を更に抑制させることができ、次亜塩素酸ガス発生装置から気相状態のガスだけを放出させることができる。
・本発明の第5の発明によれば、ナノフィルタの隙間をミストにより詰まらせにくく、ガス発生装置を長時間に亘って連続運転させても、水分放出量を抑制させることができる。
・本発明の第6の発明によれば、次亜塩素酸ガス発生装置が、長時間に亘って連続運転されても、ガス発生量の低下がされにくく、安定してガスを放出させ続けることができる。
・本発明の第7の発明によれば、ファンにより次亜塩素酸ガスを拡散させていることにより、半減周期の短い次亜塩素酸ガスをすみやかに拡散させることができ、高い濃度の次亜塩素酸ガスを片寄らせないで、気積の大きい部屋の隅々にまで薄い濃度の次亜塩素酸ガスを拡散させ、短時間でウイルスを不活化させると共に金属腐食を発生させにくい。
- According to the fourth aspect of the present invention, even solid particles such as chlorides can be removed, and the amount of water released can be further suppressed, and the gas phase state from the hypochlorous acid gas generator can be reduced. Only gas can be released.
- According to the fifth aspect of the present invention, it is difficult for mist to clog the gaps of the nanofilter, and even if the gas generator is operated continuously for a long period of time, the amount of water released can be suppressed.
・According to the sixth aspect of the present invention, even if the hypochlorous acid gas generator is continuously operated for a long time, the amount of gas generated is unlikely to decrease, and the gas can be stably and continuously released. can be done.
- According to the seventh aspect of the present invention, by diffusing the hypochlorous acid gas with the fan, the hypochlorous acid gas with a short half-life period can be rapidly diffused, and the hypochlorous acid gas with a high concentration It diffuses hypochlorous acid gas at a low concentration to every corner of a room with a large air volume without causing chloric acid gas to be concentrated, inactivating viruses in a short time and preventing metal corrosion.
・本発明の第8の発明によれば、低い湿度環境とし、新鮮な外気による換気と共に次亜塩素酸ガスを供給し、真菌類の発生を抑えた状態で消臭、除菌等が行われ、高齢者や医療対象室に適した空調システムとすることができるという従来にない有利な効果を奏する。
・本発明の第9の発明によれば、ウイルス不活化作用を有する反面、半減周期が限られている次亜塩素酸ガスが、各区画に有効に供給される建物とすることができるという効果を奏する。
・According to the eighth aspect of the present invention, a low humidity environment is provided, hypochlorous acid gas is supplied together with ventilation with fresh outside air, and deodorization, sterilization, etc. are performed in a state where the growth of fungi is suppressed. , the air conditioning system can be made suitable for the elderly and medical rooms, which is an unprecedented advantageous effect.
・According to the ninth aspect of the present invention, hypochlorous acid gas, which has a virus inactivating effect but has a limited half-life cycle, can be effectively supplied to each section. play.
次亜塩素酸ガス発生装置の説明図(実施例1)。Explanatory drawing of hypochlorous acid gas generator (Example 1). 次亜塩素酸ガスの半減周期確認試験。Confirmation test for the half-life period of hypochlorous acid gas. 相対湿度と次亜塩素酸ガス発生量との相関関係の確認試験。Confirmation test of the correlation between relative humidity and the amount of hypochlorous acid gas generated. フィルタ効果確認試験。Filter effect confirmation test. 次亜塩素酸ガス発生確認試験。Hypochlorous acid gas generation confirmation test. 液相ミスト不存在確認試験。Liquid phase mist absence confirmation test. ウイルス失活試験。Virus inactivation test. 相対湿度と次亜塩素酸ガス濃度の試験。Testing relative humidity and hypochlorous acid gas concentration. フィルタの説明図(実施例2)。Explanatory drawing of a filter (Example 2). フィルタの他の態様の説明図(実施例2)。Explanatory drawing of another aspect of a filter (Example 2). フィルタに付着した滴の図(実施例2)。FIG. 10 is a diagram of a drop adhering to a filter (Example 2). 空調システムおよび建物の説明図(実施例3)。Explanatory drawing of an air-conditioning system and a building (Example 3).
 次亜塩素酸ガス発生装置(以下、発生装置という。)に、二重の円筒壁を備えさせ、二重の円筒壁をなす外円筒壁を貯留槽から起立させると共に、その下方部を次亜塩素酸水に浸漬させ、内円筒壁の下方周囲と次亜塩素酸水面との間に隙間を備えさせるようにした。内円筒壁の内部で、次亜塩素酸水を回転する網体に、空気加圧手段により導入した空気を衝突させてミストを発生させ、ミストを内円筒壁の中では下降させ、二重の円筒壁がなす隙間空間では上昇させるようにした。 The hypochlorous acid gas generator (hereinafter referred to as the generator) is provided with a double cylindrical wall, the outer cylindrical wall forming the double cylindrical wall is erected from the storage tank, and the lower part is It was immersed in chloric acid water to provide a gap between the lower periphery of the inner cylindrical wall and the hypochlorous acid water surface. Inside the inner cylindrical wall, the air introduced by the air pressurization means collides with the rotating net body of hypochlorous acid water to generate mist, and the mist descends in the inner cylindrical wall to create a double The gap space formed by the cylindrical wall is made to rise.
 隙間空間で滴となったミストは、二重の円筒壁の間の壁面に付着され貯留槽に落下回収され、次亜塩素酸水の水面の攪乱を外円筒壁の内側だけに留め、次亜塩素酸水面からの飛沫が飛ばない外円筒壁の外方にガス放出口を備えさせ、気相状態となるミストと次亜塩素酸ガス(以下、ガスという。)のみを放散させるようにした。 The mist that becomes droplets in the gap space adheres to the wall surface between the double cylindrical walls and is dropped and collected in the storage tank. A gas discharge port is provided on the outside of the outer cylindrical wall where droplets from the chloric acid water surface do not fly, and only mist and hypochlorous acid gas (hereinafter referred to as gas) that are in a gas phase state are emitted.
 本発明の理解を容易にするため、ガスの性状を確認する第1の試験と、本発明に係る装置を使った第2の試験を説明してから、実施例を説明する。第1の試験として、「ガスの半減周期確認試験」、「相対湿度とガス発生量の相関関係の第1の確認試験」をした。第2の試験として、本装置を使った「放湿試験」、「フィルタ効果確認試験」、「ガス発生確認試験」、「液相ミスト不存在確認試験」、「インフルエンザウイルスの失活試験」、「相対湿度とガス発生量の相関関係の第2の確認試験」をした。 In order to facilitate understanding of the present invention, the first test for confirming the properties of the gas and the second test using the device according to the present invention will be explained, and then the examples will be explained. As the first tests, a "gas half-life period confirmation test" and a "first confirmation test of the correlation between the relative humidity and the amount of gas generated" were performed. As the second test, using this device, "moisture release test", "filter effect confirmation test", "gas generation confirmation test", "liquid phase mist absence confirmation test", "influenza virus deactivation test", A "second confirmation test of the correlation between the relative humidity and the amount of generated gas" was carried out.
 まず、第1の試験に使用した装置と実験環境を説明する。第1の試験では、容積1.2m3の試験容器内に、湿度調整用装置と特許文献1に記載のガス発生用装置を設置した。ガス発生用装置では、送風量が1分あたり約0.012m3の小型ファンを使っている。 First, the apparatus and experimental environment used in the first test will be described. In the first test, a humidity control device and a gas generation device described in Patent Document 1 were installed in a test container having a volume of 1.2 m 3 . The gas generator uses a small fan with an air volume of about 0.012 m 3 per minute.
 ガスの性状をより正確に確認するため、次亜塩素酸塩を精製水に溶解させてから塩化物を除去させ、pHを弱酸性に調整させた次亜塩素酸水からガスを発生させた。次亜塩素酸水の量は500mlであり、有効塩素濃度は約100ppmに調整した。試験室は20℃の試験環境とした。 In order to more accurately confirm the properties of the gas, hypochlorite was dissolved in purified water, chlorides were removed, and gas was generated from the hypochlorous acid water whose pH was adjusted to be weakly acidic. The amount of hypochlorous acid water was 500 ml, and the effective chlorine concentration was adjusted to about 100 ppm. The test room was set to a test environment of 20°C.
(ガスの半減周期確認試験)
 「ガスの半減周期確認試験」では、予め精製水だけを使って実験容器内の初期相対湿度を10%から70%まで10%ずつ変化させて計7回実施し、初期相対湿度とガスの半減周期との相関関係を確認した(図2のa点からg点)。
(Gas half-life period confirmation test)
In the "gas half-life cycle confirmation test", only purified water was used in advance, and the initial relative humidity in the experimental container was changed from 10% to 70% by 10%, and the initial relative humidity and gas were reduced by half. A correlation with the cycle was confirmed (points a to g in FIG. 2).
 所望の初期相対湿度、例えば10%としてから、試験容器内で発生装置を10分間駆動させた。10分経過後の試験容器内の最大有効塩素濃度を測定し、最大有効塩素濃度となってから有効塩素濃度が2分の1となるまでの時間(以下、半減周期という)と、その時点の最終相対湿度を測定した。試験結果を下記の表1と図2に示している。なお、各湿度における最大有効塩素濃度は異なっている。 After the desired initial relative humidity, for example 10%, the generator was driven in the test container for 10 minutes. Measure the maximum available chlorine concentration in the test container after 10 minutes, and measure the time from reaching the maximum available chlorine concentration until the available chlorine concentration becomes 1/2 (hereinafter referred to as the half-life cycle), and at that time Final relative humidity was measured. The test results are shown in Table 1 below and FIG. Note that the maximum effective chlorine concentration at each humidity is different.
[表1]
Figure JPOXMLDOC01-appb-I000001
[Table 1]
Figure JPOXMLDOC01-appb-I000001
 半減周期は、初期相対湿度を10%に調整したときが最も長く、約38分であった(表1,図2のa参照)。半減周期は、初期相対湿度が高くなるにつれて、徐々に減少し、初期相対湿度60%まで低下し、その時点の半減周期は約10分であった(表1,図2のf参照)。初期相対湿度を70%に調整したときには、半減周期は22分となった(表1,図2のg参照)。 The half-life period was the longest when the initial relative humidity was adjusted to 10%, and was about 38 minutes (see Table 1, a in Figure 2). The half-life period gradually decreased as the initial relative humidity increased, and decreased to an initial relative humidity of 60%, at which time the half-life period was about 10 minutes (see f in Table 1 and Fig. 2). When the initial relative humidity was adjusted to 70%, the half-life period was 22 minutes (see Table 1, Fig. 2g).
 ガスの半減周期が長い湿度環境とすれば、除菌対象空間にガスを長時間漂わせることができるため、ガスの濃度が薄くてもウイルス失活効果が期待できる。除菌対象空間を過度な加湿としないで、ガスの活性を維持しやすい半減周期が長い除菌対象空間の相対湿度は、50%を超えないことが好適であることが確認された。  In a humid environment with a long half-life cycle of gas, the gas can be left to float in the space to be disinfected for a long time, so even if the gas concentration is low, the virus deactivation effect can be expected. It was confirmed that the relative humidity of the space to be sterilized, which has a long half-life cycle that facilitates maintenance of gas activity, should preferably not exceed 50% without excessive humidification of the space to be sterilized.
(相対湿度とガス発生量の相関関係の第1の確認試験)
 「除菌対象空間の相対湿度とガスの発生量の相関関係」は、試験容器内の相対湿度を予め10%から70%までの湿度環境として、試験容器内で特許文献1に記載の発生装置だけを駆動させ、ガスを発生させ、ガスの発生量を測定することにより確認した。試験結果を下記の表2と図3に示している。
(First Confirmation Test of Correlation Between Relative Humidity and Gas Generation Amount)
"The correlation between the relative humidity of the space to be sterilized and the amount of gas generated" is obtained by setting the relative humidity in the test container to a humidity environment of 10% to 70% in advance, and the generator described in Patent Document 1 in the test container. was driven to generate gas, and the amount of gas generated was measured. The test results are shown in Table 2 below and FIG.
[表2]
Figure JPOXMLDOC01-appb-I000002
[Table 2]
Figure JPOXMLDOC01-appb-I000002
 この確認試験からは、相対湿度が20%のときに試験容器内のガス濃度が12.5ppbとなり、最も高い数値を示した(表2と図3のi参照)。相対湿度の上昇に伴って相対湿度50%までは、ガス発生量は同一の勾配でゆるやかに減少した。一方、相対湿度60%を超えてからはガス発生量が減少し、相対湿度70%(表2と図3のn参照)では、相対湿度20%のときの約3分の1となり、ガス発生量が著しく減少することが確認された。 From this confirmation test, the gas concentration in the test container was 12.5 ppb when the relative humidity was 20%, which was the highest value (see i in Table 2 and Fig. 3). As the relative humidity increased, the amount of gas generated gradually decreased with the same slope up to a relative humidity of 50%. On the other hand, after exceeding 60% relative humidity, the amount of gas generated decreased, and at 70% relative humidity (see n in Table 2 and Fig. 3), it was about one-third that at 20% relative humidity. It was confirmed that the amount was significantly reduced.
 ガス発生量が多く、半減周期が長い湿度領域でガスを発生させると、発生装置が小さくても大きなウイルス失活効果が期待できる。上記の2つの確認試験から、カビ等の真菌類の繁殖を抑制させたうえで、ガスを効率よく発生させ、有効活性期間を長くさせるには、水分放出量を抑えた、相対湿度が50%以下の湿度環境でガスを発生させることが好適であることが確認された。 If gas is generated in a humidity region with a large amount of gas generation and a long half-life period, a large virus deactivation effect can be expected even with a small generator. From the above two confirmation tests, in order to suppress the growth of fungi such as mold, to efficiently generate gas, and to extend the effective activity period, the amount of moisture released is suppressed, and the relative humidity is 50%. It has been found suitable to generate the gas in the following humidity environment.
 次に、第2の試験に使用した本発明に係る発生装置を説明する(図1参照)。装置の空気加圧手段は、1分あたり約1.2m3の送風能力があり、加圧能力が約147Paのシロッコファンである。第2の試験では、ジクロロイソシアヌル酸ナトリウムを水に溶解させた次亜塩素酸水からガスを発生させた。次亜塩素酸水の一回の使用量は3Lとし、次亜塩素酸水の濃度は約100ppmとした。第2の試験は、温度調整と換気のみが可能とされた床面積が約55m2、容積が約135m3の鉄筋コンクリート造の一室を試験室とし、室温を22℃に設定し実施した。 Next, the generator according to the present invention used in the second test will be described (see FIG. 1). The air pressurizing means of the apparatus is a sirocco fan with a blowing capacity of about 1.2 m 3 per minute and a pressurizing capacity of about 147 Pa. In the second test, gas was generated from hypochlorous acid water in which sodium dichloroisocyanurate was dissolved in water. The amount of hypochlorous acid water used at one time was 3 L, and the concentration of hypochlorous acid water was about 100 ppm. The second test was carried out by setting the room temperature to 22° C. in a reinforced concrete room with a floor area of about 55 m 2 and a volume of about 135 m 3 where only temperature control and ventilation were possible.
(放湿試験)
 放湿試験では、本発明の実施例1の発生装置1を使用し、6時間の連続運転を行い、残水量から除菌対象空間に放出された水分量を確認した。放湿試験は、ガス放出口にフィルタ装着なし、ナノフィルタのみ装着、不織布フィルタのみ装着、二重フィルタ装着の4つの態様で行った。
(Moisture release test)
In the moisture release test, the generator 1 of Example 1 of the present invention was used, continuous operation was performed for 6 hours, and the amount of moisture released into the sterilization target space was confirmed from the remaining amount of water. The moisture release test was conducted in four modes: no filter attached to the gas outlet, only a nanofilter attached, only a non-woven fabric filter attached, and a double filter attached.
 なお、「一般社団法人 日本電機工業会規格:JEM1426」によれば、適用床面積に応じて推奨される加湿器の定格加湿能力が規定されている。定格加湿能力とは、室温20℃、湿度30%における1時間あたりの加湿能力である。試験室の床面積が約55m2であり鉄筋コンクリート造の建物であるため、加湿器に本来求められる定格加湿能力は約1200mL/hである。以下の表3には、試験結果として6時間の水分放出量と1時間あたりの加湿能力と、前記定格加湿能力に対しての加湿比率とを示している。 According to "Japan Electrical Manufacturers' Association Standard: JEM1426", a recommended rated humidification capacity of a humidifier is defined according to the applicable floor area. The rated humidifying capacity is the humidifying capacity per hour at room temperature of 20° C. and humidity of 30%. Since the floor area of the test room is about 55 m 2 and the building is made of reinforced concrete, the rated humidifying capacity originally required for the humidifier is about 1200 mL/h. Table 3 below shows, as test results, the amount of water released for 6 hours, the humidifying capacity per hour, and the humidifying ratio with respect to the rated humidifying capacity.
[表3]
Figure JPOXMLDOC01-appb-I000003
[Table 3]
Figure JPOXMLDOC01-appb-I000003
 発生装置1は、1時間あたりの加湿能力が、水分放出量抑制手段をなすフィルタをつけなくても、215mLであり、推奨される定格加湿能力に対して僅か18%の水分放出量となった。フィルタをつけた場合には、1時間あたりの加湿能力が50mLから60mLであり、定格加湿能力に比べて4%から5%となり、極めて少量しか水分を放出しないことが確認された。 The generator 1 has a humidification capacity of 215 mL per hour without a filter that suppresses the amount of water released, which is only 18% of the recommended rated humidification capacity. . When the filter was attached, the humidification capacity per hour was 50 mL to 60 mL, which was 4% to 5% of the rated humidification capacity, and it was confirmed that only a very small amount of water was released.
(フィルタ効果確認試験)
 放出された気体が金属腐食作用に及ぼす影響の違いを、フィルタ100の種類を変えて確認するフィルタ効果確認試験を実施した(図4(A)図参照)。発生装置1のガス放出口31を種類の異なるフィルタで覆い、細線からなる銅繊維110を置き、腐食の違いを確認した。空間に暴露した状態と、100ppmの次亜塩素酸水を使用した場合の計4回の試験を実施した。いずれの試験も試験時間は2時間とした。この試験結果を以下の表4と図4に示している。図4(A)図は試験状態を示し、図4(B)図は銅繊維の写真を示している。
(Filter effect confirmation test)
A filter effect confirmation test was conducted by changing the type of the filter 100 to confirm the difference in the influence of the released gas on the metal corrosive action (see FIG. 4(A)). The gas outlet 31 of the generator 1 was covered with filters of different types, copper fibers 110 made of fine wires were placed, and differences in corrosion were confirmed. A total of four tests were carried out, one in which the specimen was exposed to the air, and the other in which 100 ppm of hypochlorous acid water was used. The test time for each test was 2 hours. The results of this test are shown in Table 4 below and in FIG. FIG. 4(A) shows a test state, and FIG. 4(B) shows a photograph of copper fibers.
[表4]
Figure JPOXMLDOC01-appb-I000004
[Table 4]
Figure JPOXMLDOC01-appb-I000004
 図4(B)図は、試験体を腐食の少ない順に並べている。銅繊維を空間に暴露させただけの場合(図4(B)図のa)には、変化がみられなかった。ガス放出口にナノフィルタを装着させ、ナノフィルタの上に銅繊維を置いた場合(図4(B)図のb)には、周縁部は変色されたが、その他の部分は金属光沢が残っていた。ガス放出口に不織布フィルタを装着させ、不織布フィルタの上に銅繊維を置いた場合(図4(B)図のc)には、全体がくすむように変色し、金属光沢も失われていた。ガス放出口にフィルタをつけないで、ガス放出口に銅繊維を吊り下げた場合には(図4(B)図のd)、全体が黒変し、金属光沢は全くない状態となった。 In Fig. 4(B), the specimens are arranged in order of least corrosion. No change was observed when the copper fibers were only exposed to the space (a in FIG. 4(B)). When a nanofilter was attached to the gas outlet and a copper fiber was placed on the nanofilter (b in FIG. 4(B)), the peripheral edge was discolored, but the metallic luster remained in other areas. was When a non-woven fabric filter was attached to the gas discharge port and copper fibers were placed on the non-woven fabric filter (Fig. 4(B), c), the overall color was dull and the metallic luster was lost. When a copper fiber was hung from the gas outlet without attaching a filter to the gas outlet (d in FIG. 4(B)), the entire surface turned black and had no metallic luster.
 この試験によれば、ナノフィルタによる場合には金属光沢が残っていたことから、次亜塩素酸水に含まれていた塩化物等の微細粒子がファンデルワールス力により取り除かれ、ナノフィルタを装着すれば微細粒子による金属の腐食が抑制できることが確認できた。また、不織布フィルタだけでは、金属腐食を抑制するこが困難であることが確認できた。 According to this test, since the metallic luster remained when using the nanofilter, fine particles such as chloride contained in the hypochlorous acid water were removed by Van der Waals force, and the nanofilter was attached. It has been confirmed that corrosion of metal due to fine particles can be suppressed by adding Moreover, it was confirmed that it is difficult to suppress metal corrosion only with a non-woven fabric filter.
(ガス発生確認試験)
 ガスが発生していることを確認する試験として、ガス放出口31に竿体200を起立させ、ガス放出口31から直近の位置、上方に20cmずつ離間した位置2か所の計3か所に、竿体200から横方向に銅繊維210を突き出させ、各位置の金属腐食によりガスの発生状態を確認している(図5(A)図参照)。試験時間は6時間としている。試験結果を表5と図5に示している。図5(A)図は、試験状態を示し、図5(B)図は銅繊維の写真を示している。
(Gas generation confirmation test)
As a test for confirming that gas is being generated, the rod body 200 was erected on the gas discharge port 31, and the rod body 200 was placed in a total of three positions: the position closest to the gas discharge port 31 and two positions spaced upward by 20 cm. , the copper fiber 210 is protruded laterally from the rod body 200, and the state of gas generation is confirmed by metal corrosion at each position (see FIG. 5A). The test time is 6 hours. Test results are shown in Table 5 and FIG. FIG. 5(A) shows a test state, and FIG. 5(B) shows a photograph of copper fibers.
[表5]
Figure JPOXMLDOC01-appb-I000005
[Table 5]
Figure JPOXMLDOC01-appb-I000005
 図5(B)図は、金属腐食が大きい順に並べている。ガス発生確認試験では、ガス放出口の直上に位置させた銅繊維(図5(B)図のa)は、全体が黒変し、金属光沢も失われていた。ガス放出口から20cm離間させた銅繊維(図5(B)図のb)は、周縁部に微かに変色がみられる程度で大部分の金属光沢は残っていた。ガス放出口から40cm離間させた銅繊維(図5(B)図のc)は、全く変色がなかった。 The figures in Fig. 5(B) are arranged in descending order of metal corrosion. In the gas generation confirmation test, the copper fiber (a in FIG. 5(B)) positioned directly above the gas discharge port was wholly blackened and lost its metallic luster. The copper fibers separated from the gas outlet by 20 cm (b in FIG. 5(B)) had a slight discoloration at the peripheral edges and most of the metallic luster remained. The copper fibers separated from the gas outlet by 40 cm (c in FIG. 5(B)) did not discolor at all.
 この試験結果から、ガス放出口からはガスが発生され、ガス放出口の直上ではガスが金属に影響を及ぼすが、ガス放出口から20cmも離間されれば、ガスが拡散され金属に対する影響は薄れ、40cm以上離間されれば、ガスが広く拡散され、フィルタなしであっても金属腐食に及ぼす影響が小さいことが確認された。 From this test result, gas is generated from the gas discharge port, and the gas affects the metal directly above the gas discharge port, but if it is separated from the gas discharge port by 20 cm, the gas diffuses and the effect on the metal diminishes. , 40 cm or more, the gas diffuses widely, and it was confirmed that the influence on metal corrosion is small even without a filter.
(液相ミスト不存在確認試験)
 ガスの放出口から出る次亜塩素酸に液相状態となるミストの放出がないことを確認する試験をした(図6参照)。併せて、次亜塩素酸により金属腐食の状態を確認している。図6(A)図は試験状態を示し、図6(B)図は銅繊維の写真を示している。ガス放出口の外側に、上方が開放された円筒状のフード部300を装着させ、銅繊維a310をフード部の内部に吊り下げ、銅繊維b320をガス流から外れた位置に横方向に突出させると共に、風に沿って、はためくようにティッシュペーパー330をフード部に添着させた(図6(A)図参照)。次亜塩素酸水は濃度100ppmとし、容量を3Lのままとしている。銅繊維b320はフード部から約15cm離間した位置とした。
(Liquid phase mist absence confirmation test)
A test was conducted to confirm that the hypochlorous acid coming out of the gas outlet did not emit liquid-phase mist (see Fig. 6). At the same time, the state of metal corrosion is confirmed with hypochlorous acid. FIG. 6(A) shows a test state, and FIG. 6(B) shows a photograph of copper fibers. A cylindrical hood part 300 with an open top is attached to the outside of the gas discharge port, the copper fiber a 310 is suspended inside the hood part, and the copper fiber b 320 is laterally protruded to a position away from the gas flow. At the same time, a tissue paper 330 was attached to the hood part so as to flutter along the wind (see FIG. 6(A)). Hypochlorous acid water has a concentration of 100 ppm, and the capacity remains at 3 L. The copper fiber b320 was positioned about 15 cm away from the hood.
 フードに被るようにして、はためいていたティシュペーパー330には、常時、全く濡れが発生せず、液相状態となるミストが発生されていないことが確認された。なお、フード部の内部に吊り下げた銅繊維aは、2時間経過時に変色が視認され、6時間経過後には全体が黒変し、金属光沢が失われた(図6(B)図)。一方、ガス放出口から15cm離間されていた銅繊維bは、6時間後にも変色はなく、金属光沢も失われていなかった。この試験によっても、ガス放出口から離間されれば、金属腐食の影響が薄れることが確認された。 It was confirmed that the tissue paper 330, which was flapping over the hood, did not get wet at all at all times, and that no liquid-phase mist was generated. In addition, the copper fiber a suspended inside the hood portion was visually discolored after 2 hours, and after 6 hours, the whole turned black and lost its metallic luster (Fig. 6(B)). On the other hand, the copper fiber b, which was separated from the gas outlet by 15 cm, showed no discoloration and no loss of metallic luster even after 6 hours. This test also confirmed that the effect of metal corrosion was reduced when the gas outlet was spaced apart.
(インフルエンザウイルスの失活試験)
 本出願人は、先の特許文献1において、インフルエンザウイルスの失活試験の結果を開示している。その試験結果によれば、相対湿度が30%から50%の除菌対象空間に、7ppbといった、極めて薄い濃度のガスを充満させただけで、インフルエンザウイルスを失活させることができることを確認している。
(Influenza virus inactivation test)
The present applicant discloses the results of an influenza virus inactivation test in the previous Patent Document 1. According to the test results, it was confirmed that the influenza virus can be deactivated simply by filling a space to be sterilized with a relative humidity of 30% to 50% with an extremely low concentration gas of 7 ppb. there is
 本出願にあたり、次亜塩素酸ガス濃度を更に薄くし、ウイルス失活試験を実施した。1.2m3の試験容器内を相対湿度30%又は50%に調整し、ガスを放散させ約2ppbとした状態で、夫々同量のインフルエンザウイルスの試験液を噴霧させ、相対湿度とガスの存在の有又は無により、どのようにウイルスが失活されるかを確認した。 For this application, the hypochlorous acid gas concentration was further reduced, and a virus inactivation test was carried out. The inside of the test container of 1.2 m 3 was adjusted to a relative humidity of 30% or 50%, and the gas was diffused to about 2 ppb. It was confirmed how the virus was inactivated by the presence or absence of
 具体的には、相対湿度30%におけるガスの放散の有又は無、相対湿度50%におけるガスの放散の有又は無の4つの場合に分け、ウイルス感染価(TCID50/mL)の減少量を確認した。ウイルス感染価の測定は、スタート直後(0分)と、15分経過時、30分経過時、45分経過時に実施した。図7には、インフルエンザウイルス失活試験の結果を示している。図7(A)図は、ウイルス感染価の経時変化を対数グラフで示し、図7(B)図は、各測定時点のウイルス感染価の実数値を示している。 Specifically, the amount of reduction in the virus infectious titer (TCID50/mL) was confirmed in four cases: with or without gas emission at a relative humidity of 30%, and with or without gas emission at a relative humidity of 50%. bottom. The virus infectivity titer was measured immediately after the start (0 minutes), and after 15 minutes, 30 minutes, and 45 minutes had passed. FIG. 7 shows the results of the influenza virus inactivation test. FIG. 7(A) shows a logarithmic graph of changes in viral infectivity over time, and FIG. 7(B) shows real values of viral infectivity at each measurement time point.
 ガスの放散無として、相対湿度30%と相対湿度50%の違いによるウイルスの感染価の減少率を比較すると、相対湿度を30%としただけの場合には(A線)、15分経過時点で約67%に減少し、30分経過時点で約31%に減少し、45分経過後には約10%に減少している。一方、相対湿度を50%としただけの場合には(B線)、15分経過時点で約21%に減少し、30分経過時点で約8%に減少し、45分経過後には約1%に減少している。 Assuming no gas diffusion, when comparing the rate of decrease in the virus infectivity due to the difference between a relative humidity of 30% and a relative humidity of 50%, when the relative humidity was only 30% (A line), after 15 minutes , decreased to about 31% after 30 minutes, and decreased to about 10% after 45 minutes. On the other hand, when the relative humidity was only 50% (line B), it decreased to about 21% after 15 minutes, decreased to about 8% after 30 minutes, and decreased to about 1% after 45 minutes. %.
 湿度30%よりも湿度50%の方が、より早くウイルスが減少されることが確認された。それに加えて相対湿度が50%の場合には、実験スタート直後の時点で、相対湿度が30%の場合に比較して、ウイルス感染価の初期値が約68%であり、減少率だけでなくウイルス感染価の初期値を抑える意味でも、湿度の役割が大きいことが確認された。 It was confirmed that the virus was reduced faster at a humidity of 50% than at a humidity of 30%. In addition, when the relative humidity was 50%, the initial value of the virus infectivity titer was about 68% immediately after the start of the experiment compared to when the relative humidity was 30%. It was confirmed that humidity plays a large role in suppressing the initial value of virus infectivity.
 次に、ガスの放散有として、相対湿度30%と相対湿度50%の違いによるウイルスの感染価の減少率を比較すると、相対湿度を30%とした場合には(C線)、15分経過時点で約10%に減少し、30分経過時点で約1.5%に減少し、45分経過後には約0.3%に減少している。一方、相対湿度を50%とした場合には(D線)、15分経過時点で約4.6%に減少し、30分経過時点で約0.32%に減少し、45分経過後には約0.07%に減少している。 Next, when comparing the rate of decrease in the virus infectivity due to the difference between 30% relative humidity and 50% relative humidity as gas diffusion, when the relative humidity is 30% (C line), 15 minutes have passed. 10% at this point, 1.5% at 30 minutes, and 0.3% at 45 minutes. On the other hand, when the relative humidity is 50% (D line), it decreases to about 4.6% after 15 minutes, to about 0.32% after 30 minutes, and after 45 minutes. It has decreased to about 0.07%.
 ガスの放散有の場合でも、湿度30%よりも湿度50%の方が、より早くウイルスが減少されることが確認されると共に、減少率だけでなくウイルス感染価の初期値を抑える意味でも、湿度の役割が大きいことが確認された。この試験を通して、相対湿度を約50%としておけば、2ppbのガスを放散させただけで、相対湿度30%でガスの放散無に比較して、ウイルス感染価をスタート直後で約32%、15分経過後で約2.2%に減少でき、著しく有利であることが確認できた。 Even in the case of gas diffusion, it was confirmed that the virus was reduced faster at a humidity of 50% than at a humidity of 30%. It was confirmed that humidity plays a large role. Through this test, with a relative humidity of about 50%, only 2 ppb of gas emission reduced the virus infectivity titer to about 32% immediately after the start, 15% compared to no gas emission at 30% relative humidity. After lapse of 10 minutes, it can be reduced to about 2.2%, which was confirmed to be extremely advantageous.
 欧州連合(EU)によれば、人が安全に生活可能な空気中の塩素ガスの環境基準は0.5ppmとされている。次亜塩素酸ガスの環境基準は定められていないため、前記の環境基準と比較すると約250分の1の濃度のガスによりウイルスを失活させることができることが確認された。 According to the European Union (EU), the environmental standard for chlorine gas in the air where people can live safely is 0.5 ppm. Since the environmental standard for hypochlorous acid gas has not been established, it was confirmed that the virus can be deactivated with a gas having a concentration of about 1/250 compared to the above environmental standard.
(相対湿度とガス発生量の相関関係の第2の確認試験)
 密閉した気積25m3の試験室を25℃とし、後述する実施例1の発生装置1を使ってガスを放散させて相対湿度とガス濃度の変化を確認した。この試験結果を図8に示している。図8(A)図はガスの濃度変化を示し、図8(B)図は試験室内の湿度変化と温度変化を示している。図8(B)図において、A線は相対湿度を示し、B線は温度を示している。相対湿度の増加に伴いガス濃度がピークとなり飽和状態を維持してから低下することが確認された。
(Second Confirmation Test of Correlation Between Relative Humidity and Gas Generation Amount)
A sealed test chamber with an air volume of 25 m 3 was set at 25° C., and gas was diffused using the generator 1 of Example 1, which will be described later, to confirm changes in relative humidity and gas concentration. The results of this test are shown in FIG. FIG. 8A shows changes in gas concentration, and FIG. 8B shows changes in humidity and temperature in the test chamber. In FIG. 8B, line A indicates relative humidity and line B indicates temperature. It was confirmed that as the relative humidity increased, the gas concentration reached a peak, maintained a saturated state, and then decreased.
 初期相対湿度は45%であった。実験スタートの湿度がガスの発生に適し、半減周期が長い湿度領域であったため、ガスは急勾配で増加し、スタート後30分で相対湿度約60%のときに最大値の約25ppbの濃度となった。「相対湿度とガス発生量の相関関係の第1の確認試験(以下、第1の確認試験という。)」で確認したように、相対湿度が50%を超えてからはガスの発生が鈍り、半減周期も短くなるため、ガス濃度は25ppbをピークとする飽和状態となり、それが約10分継続した。 The initial relative humidity was 45%. Since the humidity at the start of the experiment was suitable for gas generation and was in a humidity region with a long half-life cycle, the gas increased steeply, reaching a maximum concentration of about 25 ppb at a relative humidity of about 60% 30 minutes after the start. became. As confirmed in the "first confirmation test of the correlation between the relative humidity and the amount of gas generated (hereinafter referred to as the first confirmation test)", the generation of gas slows down after the relative humidity exceeds 50%, Since the half-life period was also shortened, the gas concentration reached a saturated state with a peak of 25 ppb, which continued for about 10 minutes.
 相対湿度が65%を超えた約40分後からは、第1の確認試験で確認したように、ガス濃度がやや低下傾向をみせ、約60分後にピークの約72%の18ppbとなった。この第2の確認試験によっても、第1の確認試験と同様に、低湿度であることがガスの発生に適していることが確認された。また、発生装置1によれば、25m3の気積の部屋でウイルスの失活が確認された2ppbの10倍以上の濃度が発生できると共に空間の相対湿度によりガス濃度を制御でき、安全かつ有効にウイルスを失活させることができることが確認できた。 About 40 minutes after the relative humidity exceeded 65%, the gas concentration tended to decrease slightly, as confirmed in the first confirmation test, and reached 18 ppb, about 72% of the peak after about 60 minutes. This second confirmation test also confirmed that low humidity is suitable for gas generation, as in the first confirmation test. In addition, according to the generator 1, it is possible to generate a concentration of 2 ppb or more that is 10 times higher than the 2 ppb in which the deactivation of the virus has been confirmed in a room with an air volume of 25 m 3 and to control the gas concentration by the relative humidity of the space, which is safe and effective. It was confirmed that the virus could be inactivated in
 実施例1では、水分放出量抑制手段を装着させた発生装置1を、図1を参照して説明する。図1(A)図は発生装置の垂直断面による説明図を示し、図1(B)図は、図1(A)図のA-A位置の水平断面図を示している。発生装置1は、次亜塩素酸ガス発生構造を備えた装置となっている。 In Example 1, the generator 1 equipped with the moisture release amount suppressing means will be described with reference to FIG. FIG. 1(A) shows a vertical sectional view of the generator, and FIG. 1(B) shows a horizontal sectional view taken along the line AA in FIG. 1(A). The generator 1 is a device having a hypochlorous acid gas generating structure.
 発生装置1は、本体部10と、本体部の上方に嵌合される内蓋20と、ガス放出口31を有する外蓋30とからなる(図1(A)図参照)。本体部10には、次亜塩素酸水の貯留槽11と、二重の円筒壁をなす外円筒壁12と、空気加圧手段13と、次亜塩素酸水のミスト化手段14と、気体導入口15と、気体導入口から前記内蓋までの気体経路とが備えられる。前記内蓋20からは内円筒壁21が垂下される。 The generator 1 consists of a main body 10, an inner lid 20 fitted above the main body, and an outer lid 30 having a gas discharge port 31 (see FIG. 1(A)). The main body 10 includes a hypochlorous acid water storage tank 11, an outer cylindrical wall 12 forming a double cylindrical wall, an air pressurization means 13, a hypochlorous acid water misting means 14, and a gas An inlet 15 and a gas path from the gas inlet to the inner lid are provided. An inner cylindrical wall 21 is suspended from the inner cover 20 .
 二重の円筒壁をなす外円筒壁12は、内円筒壁21とミスト化手段14とが同軸上に配置されるように、貯留槽の底板に分散して配設された4つのスペーサ16に載置されて位置決めされる(図1(B)図参照)。前記内蓋20には、二重の円筒壁をなす内円筒壁21と、内円筒壁21に外気を導入させる気体経路と、外円筒壁12よりも下流の気体経路に配置される垂れ壁24とが備えられる(図1(A)図参照)。内円筒壁21が垂下される長さは、次亜塩素酸水の水面との間に気体経路をなす隙間23があけられる長さとされる。 The outer cylindrical wall 12 forming a double cylindrical wall is attached to four spacers 16 dispersedly disposed on the bottom plate of the storage tank so that the inner cylindrical wall 21 and the mist generating means 14 are coaxially arranged. It is placed and positioned (see FIG. 1(B)). The inner lid 20 includes an inner cylindrical wall 21 forming a double cylindrical wall, a gas passage for introducing outside air into the inner cylindrical wall 21, and a hanging wall 24 arranged in the gas passage downstream of the outer cylindrical wall 12. are provided (see FIG. 1(A)). The length by which the inner cylindrical wall 21 hangs is set to a length that allows a gap 23 forming a gas path between the inner cylindrical wall 21 and the water surface of the hypochlorous acid water.
 内蓋が本体部の上方に嵌合されると、内蓋20から垂下された内円筒壁21と、貯留槽11から立設された外円筒壁12とが二重の円筒壁をなす。この内蓋20の上に外蓋30が被されると、気体導入口15から内円筒壁の内部、内円筒壁の下方周縁と次亜塩素酸水面との隙間23、二重の円筒壁の隙間空間26を経て、ガス放出口31に至る気体経路が形成される。ガス放出口31は、外蓋の天面に開口され、外円筒壁12の領域外に位置している(図1参照)。 When the inner lid is fitted above the main body, the inner cylindrical wall 21 suspended from the inner lid 20 and the outer cylindrical wall 12 erected from the reservoir 11 form a double cylindrical wall. When the outer lid 30 is placed on the inner lid 20, the inside of the inner cylindrical wall from the gas inlet 15, the gap 23 between the lower peripheral edge of the inner cylindrical wall and the hypochlorous acid water surface, and the double cylindrical wall A gas path is formed that reaches the gas discharge port 31 through the gap space 26 . The gas discharge port 31 is opened in the top surface of the outer lid and positioned outside the area of the outer cylindrical wall 12 (see FIG. 1).
 空気加圧手段13により、気体導入口15から空気が加圧誘導されると、内蓋20に形成された気体経路を通じて、ミストを発生させる内円筒壁21の内部空間に空気が導入され、内部空間に沿ってミスト混じりの空気が下降される。加圧誘導されるミストと外気は降下され、内円筒壁の下方と水面との間の周囲の隙間23から、内円筒壁と外円筒壁との間の隙間空間26に均等に流れ、隙間空間26を上昇する。このときに、隙間空間26で滴となったミストが、内円筒壁と外円筒壁との間の壁面に付着され貯留槽11に落下回収される。 When air is pressurized and induced from the gas inlet 15 by the air pressurizing means 13, the air is introduced through the gas path formed in the inner lid 20 into the inner space of the inner cylindrical wall 21 that generates mist. Air mixed with mist descends along the space. The pressurized mist and the outside air are lowered, and flow uniformly from the peripheral gap 23 between the bottom of the inner cylindrical wall and the water surface to the gap space 26 between the inner and outer cylindrical walls, and the gap space Ascend 26. At this time, the mist formed into droplets in the clearance space 26 adheres to the wall surface between the inner cylindrical wall and the outer cylindrical wall and is dropped and collected in the storage tank 11 .
 気相状態をなすミストとガスは、外円筒壁12の上部まで上昇してから、内蓋の開口孔27に向かい、開口孔27から内蓋と外蓋の間の空間に導入されガス放出口31に至り、除菌対象空間に放出される。ミストが加圧空気で気体経路を誘導されている間に、液相状態をなす次亜塩素酸が貯留槽11に落下され、気相状態となる次亜塩素酸だけがガス放出口に至り、前述した放湿試験のとおり、除菌対象空間への水分放出量が抑制される(表3参照)。 The gas-phase mist and gas rise to the upper portion of the outer cylindrical wall 12, head toward the opening 27 of the inner lid, and are introduced through the opening 27 into the space between the inner and outer lids, where they exit the gas discharge port. 31 and is released into the space to be sterilized. While the mist is guided through the gas path by the pressurized air, hypochlorous acid in a liquid phase is dropped into the storage tank 11, and only the hypochlorous acid in a gaseous state reaches the gas outlet, As in the moisture release test described above, the amount of moisture released into the space to be sterilized is suppressed (see Table 3).
 なお、気体経路を横断する垂れ壁24を内蓋に備えさせておくと、外円筒壁の領域外でも、微細なミストのうち液相状態をなすミストが垂れ壁24により滴となり、貯留槽11に落下回収される。垂れ壁24に至る時点では液相状態となるミストの大半が除去されているが、垂れ壁24を設けることによっても、水分発生量を更に抑制させることができる。 If the inner lid is provided with a hanging wall 24 that traverses the gas path, fine mist in a liquid state becomes droplets by the hanging wall 24 even outside the region of the outer cylindrical wall, and the storage tank 11 to be recovered. Although most of the mist in the liquid state is removed when it reaches the hanging wall 24, the provision of the hanging wall 24 can further suppress the amount of water generated.
 貯留槽11の下方には、ミスト化手段14の駆動部等を備えさせると共に、次亜塩素酸水タンク22の格納場所としておけばよい。スペーサ16に外円筒壁12を載置させ、次亜塩素酸水の貯留槽11を外円筒壁の内外で連通させているため、外円筒壁の外に落下した滴も外円筒壁の内に落下した滴も貯留槽11に回収される。外円筒壁12の下方が貯留槽11に浸漬された状態とされているため、外円筒壁の内の水面の撹乱の影響が、外円筒壁の領域外には及ばない(図1(A)図参照)。 The lower part of the storage tank 11 may be provided with a drive unit for the misting means 14 and as a storage place for the hypochlorous acid water tank 22 . Since the outer cylindrical wall 12 is placed on the spacer 16, and the hypochlorous acid water storage tank 11 is communicated between the inside and the outside of the outer cylindrical wall, drops that fall outside the outer cylindrical wall also enter the outer cylindrical wall. Droplets that have fallen are also collected in the storage tank 11 . Since the lower part of the outer cylindrical wall 12 is immersed in the reservoir 11, the disturbance of the water surface inside the outer cylindrical wall does not affect the area outside the outer cylindrical wall (Fig. 1A). (see diagram).
 また、外円筒壁12と内蓋20の側壁17とは、気体が流通できる隙間25が離間されている(図1(B)図参照)。二重の円筒壁の隙間空間26からガス放出口31とは反対側に誘導された次亜塩素酸ミストは、外円筒壁12と側壁17の隙間25を迂回してガス放出口31に誘導される。外円筒壁12の高さは、内蓋20を本体部10に嵌合させたときに、内蓋20と外円筒壁12とが離間され、気体経路が形成される高さとしている。 Also, the outer cylindrical wall 12 and the side wall 17 of the inner lid 20 are separated by a gap 25 through which gas can flow (see FIG. 1(B)). The hypochlorous acid mist guided from the gap space 26 between the double cylindrical walls to the side opposite to the gas discharge port 31 bypasses the gap 25 between the outer cylindrical wall 12 and the side wall 17 and is guided to the gas discharge port 31. be. The height of the outer cylindrical wall 12 is such that when the inner lid 20 is fitted to the main body 10, the inner lid 20 and the outer cylindrical wall 12 are separated from each other to form a gas passage.
 空気加圧手段13は、ガス放出口31にフィルタを装着させた場合でも、ガスを放出することができるように、フィルタによる圧力損失に応じたファンが選択されればよく、加圧能力と形態は限定されないが、送風量が最大で1.2m3/分のシロッコファンとしている。このシロッコファンによれば、発生装置の内部を約150Paの圧力で加圧することができ、二重のフィルタを装着させても、ガスが放出可能である。 As the air pressurizing means 13, a fan corresponding to the pressure loss caused by the filter may be selected so that the gas can be released even when a filter is attached to the gas outlet 31. is not limited, but a sirocco fan with a maximum blowing volume of 1.2 m 3 /min. According to this sirocco fan, the inside of the generator can be pressurized at a pressure of about 150 Pa, and gas can be discharged even if a double filter is attached.
 次亜塩素酸水のミスト化手段14は、二重の円筒壁と同軸上に配され、放散手段18と円筒状の網体19と、これらを一体に回転させる駆動部とされる。放散手段18は断面積が下方に向けて小さくなる漏斗体とされ、漏斗体の下端開口部が貯留槽11に浸漬され、上端部が蓋部材で閉塞されると共に上部周縁部に液滴の放散口28が放射状に配列されている。また漏斗体の上端部には径方向に突出される鍔部29が備えられ、鍔部29の外縁から円筒状の網体19が垂下される。 The hypochlorous acid water misting means 14 is arranged coaxially with the double cylindrical wall, and is composed of a dispersing means 18, a cylindrical mesh body 19, and a driving part that rotates them integrally. The diffusing means 18 is a funnel whose cross-sectional area decreases toward the bottom. The lower end opening of the funnel is immersed in the storage tank 11, the upper end is closed with a lid member, and the liquid droplets scatter around the upper peripheral edge. The openings 28 are arranged radially. A radially protruding brim 29 is provided at the upper end of the funnel, and a cylindrical mesh 19 hangs down from the outer edge of the brim 29 .
 網体19は、ステンレス製の網体とされ、メッシュ径が約1mmとされる。放散手段18と網体19とは一体に回転される。放散手段18と網体19とが回転されると、放散手段をなす漏斗体の内面に沿って次亜塩素酸水がくみ上げられ、放散口28から液滴となって放散され、回転する網体19に衝突される。 The mesh body 19 is made of stainless steel and has a mesh diameter of about 1 mm. The dissipating means 18 and the mesh 19 are rotated integrally. When the dissipating means 18 and the mesh body 19 are rotated, the hypochlorous acid water is pumped up along the inner surface of the funnel body forming the dissipating means, is dispersed as droplets from the dispersing port 28, and is rotated. 19 will collide.
 液滴が網体19に衝突されて破砕されることにより、内円筒壁21の中に次亜塩素酸ミストを発生させるため、効率よく次亜塩素酸ミストを発生させることができる。ミストにならなかった液相状態の次亜塩素酸水は、放散された勢いで内円筒壁21の壁面に付着され、壁面に沿って垂れ落ち、大部分が貯留槽11に落下して回収される。 Since the hypochlorous acid mist is generated in the inner cylindrical wall 21 by the droplets collided with the mesh 19 and crushed, the hypochlorous acid mist can be generated efficiently. The hypochlorous acid water in the liquid phase state that did not become mist adheres to the wall surface of the inner cylindrical wall 21 due to the force of diffusion, drips down along the wall surface, and most of it falls into the storage tank 11 and is collected. be.
 実施例2では、発生装置のガス放出口31に水分放出量抑制手段をなすフィルタ40を装着させ、ガス放出口にガス拡散手段41を設けた発生装置2を、図9から図11を参照して説明する。図9(A)図は、その構成を示し、図9(B)図は、第1の水分放出量抑制手段をなす不織布フィルタの拡大図を示している。図9では、理解を容易にするため、フィルタ40とガス拡散手段41だけを実線で示し、発生装置の他の構成を破線で示している。 In Example 2, the gas outlet 31 of the generator is fitted with a filter 40 serving as a means for suppressing the amount of water released, and the gas outlet is provided with a gas diffusion means 41. The generator 2 is shown in FIGS. to explain. FIG. 9(A) shows the configuration thereof, and FIG. 9(B) shows an enlarged view of a non-woven fabric filter that constitutes the first moisture release suppressing means. In FIG. 9, in order to facilitate understanding, only the filter 40 and the gas diffusion means 41 are indicated by solid lines, and other configurations of the generator are indicated by broken lines.
 図10はフィルタの他の態様を示している。図10(A)は、第2の水分放出量抑制手段をなすナノフィルタ50を示し、図10(B)図,図10(C)図には第3の水分放出量抑制手段をなす二重のフィルタを示している。図11(A)図は、図9(A)図の態様の不織布フィルタ40の上流面の写真を示し、図11(B)図は、図10(A)図のナノフィルタ50の上流面の拡大写真を示している。 FIG. 10 shows another aspect of the filter. FIG. 10(A) shows a nanofilter 50 forming the second moisture release suppressing means, and FIGS. shows a filter for FIG. 11(A) shows a photograph of the upstream surface of the non-woven fabric filter 40 in the embodiment of FIG. 9(A), and FIG. 11(B) shows a photograph of the upstream surface of the nanofilter 50 of FIG. 10(A). A magnified photo is shown.
 発生装置2には、ガス放出口に、空気加圧手段の性能等に応じて、いずれかの態様のフィルタが装着されればよい。フィルタを装着させるとガス放出口からのガスの放出速度が低下され、ガスが放出口近く又は低い位置に滞留されるため、ガス放出口のフィルタ面に沿ってガス拡散手段をなすファンを備えさせ、除菌対象空間の広い範囲に、短時間でガスを拡散させるようにしている。 The generator 2 may be fitted with any type of filter at the gas outlet depending on the performance of the air pressurizing means. When the filter is attached, the speed of gas discharge from the gas discharge port is reduced and the gas is retained near or at a low position. Therefore, a fan serving as a gas diffusion means is provided along the filter surface of the gas discharge port. , the gas is diffused in a short time over a wide range of the space to be sterilized.
 いずれの態様のフィルタも、ゴム製のパッキング42等でガス放出口に気密に装着させることにより、ガスがフィルタ部分のみを通過して除菌対象空間に放出される。フィルタを装着させると、装置内部の圧力が高まり、本体、内蓋、外蓋の境界部分から、次亜塩素酸が漏出されることがあるため、空気導入口からガス放出口までの気体経路以外は気密にさせるとよい(図9(A)図参照)。 By air-tightly attaching the filter of either aspect to the gas discharge port with a rubber packing 42 or the like, the gas passes only through the filter portion and is discharged into the sterilization target space. When the filter is attached, the pressure inside the device increases, and hypochlorous acid may leak from the boundary between the main body, the inner lid, and the outer lid. should be airtight (see FIG. 9(A)).
 第1の水分放出量抑制手段(図9(B)図参照)は、人に着用される不織布マスクと同等の撥水処理がされた不織布フィルタとしている。具体的には、フィルタをなす繊維の繊維径が1μm以上6μm以下で圧力損失が約30Paである。ここでは、不織布フィルタを折り曲げずに、全体を平坦なままガス放出口31に、次亜塩素酸ミストが漏れないように装着させている。例えば、フィルタの周囲にゴム製のパッキング42等を備えさせ、ガス放出口に密着させて気密性を確保させればよい。 The first water release amount suppressing means (see FIG. 9(B)) is a non-woven fabric filter that has undergone water-repellent treatment equivalent to that of a non-woven fabric mask worn by a person. Specifically, the fibers forming the filter have a fiber diameter of 1 μm or more and 6 μm or less and a pressure loss of about 30 Pa. In this case, the non-woven fabric filter is not bent and is attached to the gas discharge port 31 in a flat state so that the hypochlorous acid mist does not leak. For example, a rubber packing 42 or the like may be provided around the filter and brought into close contact with the gas discharge port to ensure airtightness.
 フィルタをなす繊維の材質は、ポリプロピレン樹脂繊維、ポリエステル樹脂繊維、ポリウレタン樹脂繊維、またはこれらの混合樹脂繊維等であればよいが限定されない。不織布フィルタの製造方法は撥水処理がされていれば限定されず、例えばメルトブローン製法、スパンボンド製法等であればよい。 The material of the fiber forming the filter may be polypropylene resin fiber, polyester resin fiber, polyurethane resin fiber, or mixed resin fiber of these, but is not limited. The manufacturing method of the non-woven fabric filter is not limited as long as it is water-repellent, and may be, for example, a meltblown manufacturing method, a spunbond manufacturing method, or the like.
 発生装置に、不織布フィルタを装着させて6時間連続運転させたときには、不織布フィルタの上流面全体が濡れた状態となっていた(図11(A)図参照)。なお、不織布フィルタの下流側の面は濡れていなかった。前記放湿試験に示したように水分放出量を抑制させると共に、前記ガス発生試験に示したようにガスを発生させていた。なお、フィルタの圧力損失は20Pa以上60Pa以下であればよく、フィルタの繊維径は1μm以上30μm以下であればよく、人に着用される不織布マスクでなくてもよいことは勿論のことである。 When the nonwoven fabric filter was attached to the generator and the generator was operated continuously for 6 hours, the entire upstream surface of the nonwoven fabric filter was wet (see Fig. 11 (A)). The downstream surface of the nonwoven fabric filter was not wet. As shown in the moisture release test, the amount of released water was suppressed, and gas was generated as shown in the gas generation test. The pressure loss of the filter should be 20 Pa or more and 60 Pa or less, the fiber diameter of the filter should be 1 μm or more and 30 μm or less, and the mask need not necessarily be a non-woven fabric mask worn by people.
 第2の水分放出量抑制手段(図10(A)図参照)は、フィルタをなすナノファイバーの繊維径が70nm以上200nm以下で圧力損失が20Pa以上60Pa未満の疎水性のナノフィルタであり、上流面が下方に凸の傾斜面をなすように、中央部で1回折り曲げられている(図10(A)図参照)。ナノフィルタは、ナノファイバーが密集された三次元網目層51と、両側の形状保持層をなす薄層の不織布52からなる三層構造のナノフィルタ50としている。 The second water release amount suppressing means (see FIG. 10A) is a hydrophobic nanofilter having a fiber diameter of 70 nm or more and 200 nm or less and a pressure loss of 20 Pa or more and less than 60 Pa. The surface is bent once at the central portion so as to form a downwardly convex inclined surface (see FIG. 10(A)). The nanofilter is a three-layer structure nanofilter 50 composed of a three-dimensional mesh layer 51 in which nanofibers are densely packed and thin nonwoven fabric layers 52 forming shape-retaining layers on both sides.
 長時間の連続運転により上流面で滴となったミストは、傾斜面に沿って中央部に集まり、貯留槽11に落下されて回収される。発生装置にナノフィルタを装着させて6時間連続運転させたときは、ナノフィルタの上流面に通過しなかったミストが微細な滴aとなり付着され、大きな滴は落下された状態とされ(図11(B)図参照)、前記放湿試験に示したように、水分放出量が抑制された。なお、下流側の面は湿った状態とはなっていなかった。 The mist that forms droplets on the upstream surface due to long-term continuous operation gathers in the center along the inclined surface and drops into the storage tank 11 to be collected. When the nanofilter was attached to the generator and it was operated continuously for 6 hours, the mist that did not pass through the upstream surface of the nanofilter adhered to the upstream surface of the nanofilter as fine droplets a, and the large droplets were dropped (Fig. 11). (B), as shown in the moisture release test, the moisture release amount was suppressed. Note that the downstream surface was not wet.
 第3の水分放出量抑制手段(図10(B)図、図10(C)図参照)は、不織布フィルタ61,62とナノフィルタ50からなる二重のフィルタとされ、夫々のフィルタの間が5mm以上離間された空間63としている。二重のフィルタは、不織布フィルタ61,62が傾斜されて枠体に装着されることにより、上流面を傾斜面とさせている。平坦な不織布フィルタ61を使用する場合には、不織布フィルタ全体を斜めに傾斜させればよい(図10(B)図参照)。この場合には、不織布に付着した滴が傾斜面に沿って周縁部に集まり速やかに落下される。 The third moisture release suppressing means (see FIGS. 10B and 10C) is a double filter composed of nonwoven fabric filters 61 and 62 and a nanofilter 50, and the space between the filters is A space 63 separated by 5 mm or more is provided. In the double filter, the non-woven fabric filters 61 and 62 are inclined and attached to the frame so that the upstream surface is an inclined surface. When using a flat nonwoven fabric filter 61, the entire nonwoven fabric filter may be inclined (see FIG. 10(B)). In this case, droplets adhering to the nonwoven fabric gather at the peripheral edge along the inclined surface and quickly drop.
 蛇腹状に屈曲させた不織布フィルタ62を使用する場合には、上流面に筋状の谷折り部ができ、不織布に付着した滴は、谷折り部に集まり落下される(図10(C)図)。いずれの場合も、不織布フィルタの内部まで濡れにくい。なお、不織布フィルタを通過する粒径のミストや、不織布フィルタの上流側が濡れたときに、通気により下流側に水分微粒子が吹き込んだとしても、不織布フィルタとナノフィルタとの空間63で気化されやすいため、ナノフィルタは乾燥状態に維持される。 In the case of using a nonwoven fabric filter 62 bent in a bellows shape, streak-like valley folds are formed on the upstream surface, and droplets adhering to the nonwoven fabric gather in the valley folds and fall (Fig. 10(C)). ). In either case, the interior of the non-woven fabric filter is not easily wetted. It should be noted that even if mist having a particle size that passes through the non-woven fabric filter, or when the upstream side of the non-woven filter gets wet, even if water fine particles are blown into the downstream side by ventilation, they are likely to be vaporized in the space 63 between the non-woven fabric filter and the nanofilter. , the nanofilter is kept dry.
 実施例3では、各階の空調経路に、次亜塩素酸ガス発生構造を備えた空調システム4を配設した建物5を、図12を参照して説明する。図12(A)図は、空調システム4の構成を説明する説明図を示し、図12(B)図は建物5の説明図を示している。次亜塩素酸ガス発生構造の構成は、実施例1の次亜塩素酸ガス発生装置と同様であるため、図12(A)では、次亜塩素酸ガス発生装置1と同一の機能を有する構成については同一の符合を付して簡単に説明する。 In Example 3, a building 5 in which an air conditioning system 4 having a hypochlorous acid gas generating structure is installed in the air conditioning path of each floor will be described with reference to FIG. FIG. 12A shows an explanatory diagram explaining the configuration of the air conditioning system 4, and FIG. 12B shows an explanatory diagram of the building 5. FIG. Since the configuration of the hypochlorous acid gas generating structure is the same as that of the hypochlorous acid gas generator of Example 1, in FIG. will be given the same reference numerals and will be briefly described.
 空調システム4は、外気を導入し居室に配給する空調経路80に備えられる。図12(A)図に一点破線で囲った範囲の空調システム4とすればよいが、貯留槽11への供給経路81を設けて、塩化ナトリウム水溶液を供給し生成装置82により電気分解して次亜塩素酸水としてもよく、次亜塩素酸水を直接供給させてもよいことは勿論のことである。 The air conditioning system 4 is provided in an air conditioning path 80 that introduces outside air and distributes it to living rooms. The air-conditioning system 4 in the range enclosed by the dashed line in FIG. 12(A) may be provided. Chlorous acid water may be used, and hypochlorous acid water may be directly supplied.
 空調システム4は、主たる空調経路80から一部を分岐させ空気を導入し、空気加圧手段13により加圧した空気を内円筒壁21の中に導入し、内円筒壁21の中において、回転される円筒状の網体と次亜塩素酸水の放散手段とからなるミスト化手段14により、微細な次亜塩素酸ミストを発生させて、空気をミストと共に内円筒壁21の中の空間を一旦下降させてから、内円筒壁と外円筒壁12の間の隙間空間26を気相状態となる次亜塩素酸を上昇させる。 The air conditioning system 4 introduces air by branching a part from the main air conditioning path 80, introduces the air pressurized by the air pressurizing means 13 into the inner cylindrical wall 21, and rotates in the inner cylindrical wall 21. A fine hypochlorous acid mist is generated by a misting means 14 consisting of a cylindrical mesh body and hypochlorous acid water diffusion means, and the space in the inner cylindrical wall 21 is filled with the air and the mist. After the hypochlorous acid is lowered once, the hypochlorous acid in the gaseous state is raised in the gap space 26 between the inner cylindrical wall and the outer cylindrical wall 12 .
 内円筒壁21の中の空間で滴となるミストを回収させてから、次亜塩素酸水の貯留槽11の水面から飛沫が発生しない外円筒壁12の領域外の上部に設けられたガス放出口83から、気相状態となる次亜塩素酸水のミストと次亜塩素酸ガスを主たる空調経路80に供給させる。主たる空調経路に供給された次亜塩素酸ガスは、予め温度・湿度が調整された空気と合流されて居室に供給される。 After recovering the mist that becomes droplets in the space in the inner cylindrical wall 21, the gas outlet provided in the upper part outside the area of the outer cylindrical wall 12 where droplets do not occur from the water surface of the hypochlorous acid water storage tank 11. From the outlet 83, mist of hypochlorous acid water and hypochlorous acid gas in gaseous state are supplied to the main air conditioning path 80. - 特許庁The hypochlorous acid gas supplied to the main air-conditioning route is combined with air whose temperature and humidity have been adjusted in advance, and is supplied to the living room.
 次亜塩素酸ガスは、湿度によって半減周期が異なるため、次亜塩素酸ガスの発生量が多く半減周期が長い相対湿度30%~50%に調整した空気を導入して、次亜塩素酸ガスを発生させて供給するのが好適であるが限定されない。ウイルス失活効果が活用できる濃度の次亜塩素酸ガスを、湿度に応じた半減周期の期間に応じて供給できる範囲を一つの区画として、建物5の人が滞在する空間を分割して、空調システム4を備えさせればよい。 Hypochlorous acid gas has a different half-life cycle depending on humidity. is preferably generated and supplied, but is not limited thereto. The space where people stay in building 5 is divided into areas where hypochlorous acid gas with a concentration that can utilize the virus deactivation effect can be supplied according to the period of the half-life cycle according to the humidity, and air conditioning is performed. The system 4 should be provided.
 建物5においては、理解を容易にするため、各階毎に空調システム4を備えさせている(図12(B)図参照)。一つの階の空調面積が大きい場合には、一つの階に複数の空調システムを備えさせるとよい。空調システム4により、相対湿度30%~60%の湿度環境として、次亜塩素酸ガスを供給することにより、真菌類の黴の発生が抑えられ、ウイルス失活効果、消臭、除菌効果も期待できる。空調システム4は、大きな事務室だけでなく、高齢者用の居室を数多く有する建物に適用でき、建物利用者に快適・安心できる空間を提供することができる。 In the building 5, each floor is equipped with an air conditioning system 4 for easy understanding (see FIG. 12(B)). If the air-conditioned area of one floor is large, it is preferable to equip one floor with a plurality of air-conditioning systems. By supplying hypochlorous acid gas in a humidity environment with a relative humidity of 30% to 60% by the air conditioning system 4, the generation of fungal mold is suppressed, and the virus deactivation effect, deodorizing effect, and sterilization effect are also achieved. I can expect it. The air conditioning system 4 can be applied not only to large offices but also to buildings having many rooms for the elderly, and can provide building users with a comfortable and safe space.
(その他)
・気体についての「ppm」は体積百万分率の単位であり、液体についての「ppm」は質量百万分率の単位であり、気体についての「ppb」は体積十億分率の単位である。
・発生装置では、予め生成させた次亜塩素酸水を使用する例を説明したが、電気分解手段を備えさせ、塩化ナトリウム水溶液を電気分解させて、次亜塩素酸水を生成させてもよいことは勿論のことである。
・今回開示された実施の形態はすべての点で例示であって、制限的なものではないと考えられるべきである。本発明の技術的範囲は、上記した説明に限らず、請求の範囲と均等の意味および範囲内でのすべての変更が含まれることが意図される。
(others)
"ppm" for gases is in parts per million by volume, "ppm" for liquids is in parts per million by mass, and "ppb" for gases is in parts per billion by volume. be.
・In the generator, an example of using pre-generated hypochlorous acid water was explained, but an electrolysis means may be provided to electrolyze the sodium chloride aqueous solution to generate hypochlorous acid water. It goes without saying.
- The embodiments disclosed this time are illustrative in all respects and should be considered not restrictive. The technical scope of the present invention is not limited to the above description, but is intended to include all modifications within the meaning and scope of equivalents to the claims.
1,2…次亜塩素酸ガス発生装置、4…空調システム、5…建物、
100…フィルタ、110…銅繊維、200…竿体、210…銅繊維、
300…フード部、310…銅繊維a、320…銅繊維b、
330…ティッシュペーパー、
10…本体部、11…貯留槽、12…外円筒壁、13…空気加圧手段、
14…ミスト化手段、15…気体導入口、16…スペーサ、17…側壁、
18…放散手段、19…網体、
20…内蓋、21…内円筒壁、22…次亜塩素酸水タンク、23…隙間、
24…垂れ壁、25…隙間、26…隙間空間、27…開口孔、28…放散口、
29…鍔部、30…外蓋、31…ガス放出口、
40…フィルタ、41…ガス拡散手段、42…パッキング、
50…ナノフィルタ、51…三次元網目層、52…不織布、
61…不織布フィルタ,62…不織布フィルタ、63…空間、
80…空調経路、81…供給経路、82…次亜塩素酸生成装置、83…ガス放出口
1, 2... Hypochlorous acid gas generator, 4... Air conditioning system, 5... Building,
DESCRIPTION OF SYMBOLS 100... Filter, 110... Copper fiber, 200... Rod body, 210... Copper fiber,
300... Hood portion, 310... Copper fiber a, 320... Copper fiber b,
330... tissue paper,
DESCRIPTION OF SYMBOLS 10... Main-body part, 11... Storage tank, 12... Outer cylindrical wall, 13... Air pressurization means,
14...Misting means, 15...Gas introduction port, 16...Spacer, 17...Side wall,
18... Diffusion means, 19... Net body,
20... Inner lid, 21... Inner cylindrical wall, 22... Hypochlorous acid water tank, 23... Gap,
24... Hanging wall, 25... Gap, 26... Gap space, 27... Opening hole, 28... Radiation port,
29... brim portion, 30... outer lid, 31... gas discharge port,
40... Filter, 41... Gas diffusion means, 42... Packing,
50... Nanofilter, 51... Three-dimensional network layer, 52... Non-woven fabric,
61...Nonwoven fabric filter, 62...Nonwoven fabric filter, 63...Space,
80... Air-conditioning route, 81... Supply route, 82... Hypochlorous acid generator, 83... Gas discharge port

Claims (9)

  1.  気相状態の次亜塩素酸のみを発生させる次亜塩素酸ガス発生構造において、
     前記次亜塩素酸ガス発生構造が、次亜塩素酸水の貯留槽と、二重の円筒壁と、気体経路と、空気加圧手段と、次亜塩素酸水のミスト化手段と、ガス放出口とを含み、
     二重の円筒壁をなす外円筒壁が、前記貯留槽から起立されると共に下方部が次亜塩素酸水に浸漬され、
     二重の円筒壁をなす内円筒壁が、その下方周囲と前記貯留槽の次亜塩素酸水面との間に隙間を備えるように垂下されて、内円筒壁の内部を気体経路となし、
     前記貯留槽が、前記外円筒壁の内外に貫通され、
     前記空気加圧手段が、気体導入口から、内円筒壁の内部を通してガス放出口まで外気を加圧誘導させ、
     前記ミスト化手段が、円筒状の網体と、次亜塩素酸水の放散手段を備え、
     前記網体が、二重の円筒壁と同心をなして回転され、
     前記放散手段が、前記内円筒壁の内部で前記網体に、次亜塩素酸水を衝突させてミストを発生させ、
     液相状態の次亜塩素酸水が、前記内円筒壁の内部で前記貯留槽に落下回収され、
     気相状態となる前記ミストが、前記隙間の周囲から前記二重の円筒壁がなす隙間空間に誘導されて上昇し、
     前記ミストが上昇している間に、前記隙間空間において滴となったミストが、前記隙間空間の領域で前記貯留槽に落下回収され、
     前記ガス放出口が、前記外円筒壁の領域外の上部に備えられ、
     前記ガス放出口から、気相状態となるミストと次亜塩素酸ガスのみが放出される、
    ことを特徴とする次亜塩素酸ガス発生構造。
    In the hypochlorous acid gas generating structure that generates only hypochlorous acid in the gas phase state,
    The hypochlorous acid gas generating structure includes a hypochlorous acid water storage tank, a double cylindrical wall, a gas path, an air pressurization means, a hypochlorous acid water misting means, and a gas discharge. including an exit and
    The outer cylindrical wall forming a double cylindrical wall is erected from the storage tank and the lower part is immersed in hypochlorous acid water,
    an inner cylindrical wall forming a double cylindrical wall is suspended so as to provide a gap between its lower periphery and the hypochlorous acid water surface of the reservoir, and the interior of the inner cylindrical wall serves as a gas passage;
    The storage tank penetrates inside and outside the outer cylindrical wall,
    The air pressurizing means pressurizes and guides external air from the gas introduction port to the gas discharge port through the interior of the inner cylindrical wall,
    The misting means comprises a cylindrical net body and hypochlorous acid water dispersing means,
    the mesh is rotated concentrically with the double cylindrical wall;
    The diffusing means causes hypochlorous acid water to collide with the mesh inside the inner cylindrical wall to generate mist,
    Hypochlorous acid water in a liquid phase is dropped and collected in the storage tank inside the inner cylindrical wall,
    the mist in the gas phase state rises by being guided from the periphery of the gap to the gap space formed by the double cylindrical walls;
    While the mist is rising, the mist that has become droplets in the gap space is dropped and collected in the storage tank in the area of the gap space,
    The gas outlet is provided at the top outside the area of the outer cylindrical wall,
    From the gas outlet, only mist and hypochlorous acid gas in a gaseous state are released,
    A hypochlorous acid gas generating structure characterized by:
  2.  次亜塩素酸ガス発生装置において、
     気相状態の次亜塩素酸のみを発生させる次亜塩素酸ガス発生装置であって、
     請求項1の記載の次亜塩素酸ガス発生構造を備えている、
    ことを特徴とする次亜塩素酸ガス発生装置。
    In the hypochlorous acid gas generator,
    A hypochlorous acid gas generator that generates only hypochlorous acid in a gaseous state,
    Equipped with the hypochlorous acid gas generating structure according to claim 1,
    A hypochlorous acid gas generator characterized by:
  3.  前記ガス放出口には、第1の水分放出量抑制手段が装着可能とされると共に、前記気体経路の気体導入口から前記ガス放出口までが気密とされ、
     第1の水分放出量抑制手段が、繊維径が1μm以上30μm以下であると共に圧力損失が20Pa以上60Pa以下である撥水性を有する不織布フィルタとされている、
    ことを特徴とする請求項2に記載の次亜塩素酸ガス発生装置。
    A first moisture release suppressing means can be attached to the gas outlet, and the gas path from the gas introduction port to the gas outlet is airtight,
    The first water release amount suppressing means is a non-woven fabric filter having a fiber diameter of 1 μm or more and 30 μm or less and a pressure loss of 20 Pa or more and 60 Pa or less, and having water repellency.
    The hypochlorous acid gas generator according to claim 2, characterized in that:
  4.  前記ガス放出口には、第2の水分放出量抑制手段が装着可能とされると共に、前記気体経路の気体導入口から前記ガス放出口までが気密とされ、
     第2の水分放出量抑制手段が、繊維径が70nm以上200nm以下の疎水性ナノファイバーを含むと共に圧力損失が20Pa以上60Pa以下のナノフィルタとされている、
    ことを特徴とする請求項2に記載の次亜塩素酸ガス発生装置。
    A second moisture release suppressing means can be attached to the gas discharge port, and a portion from the gas introduction port of the gas path to the gas discharge port is airtight,
    The second water release amount suppressing means is a nanofilter containing hydrophobic nanofibers having a fiber diameter of 70 nm or more and 200 nm or less and having a pressure loss of 20 Pa or more and 60 Pa or less.
    The hypochlorous acid gas generator according to claim 2, characterized in that:
  5.  前記ガス放出口には、第3の水分放出量抑制手段が装着可能とされると共に、前記気体経路の気体導入口から前記ガス放出口までが気密とされ、
     第3の水分放出量抑制手段が、上流側から、繊維径が1μm以上30μm以下であると共に圧力損失が20Pa以上60Pa以下である撥水性を有する不織布フィルタと、繊維径が70nm以上200nm以下の疎水性ナノファイバーを含むと共に圧力損失が20Pa以上60Pa以下のナノフィルタからなる二重のフィルタとされ、二重のフィルタの間が少なくとも5mm以上離間されている、
    ことを特徴とする請求項2に記載の次亜塩素酸ガス発生装置。
    A third means for suppressing the amount of water released can be attached to the gas outlet, and a portion from the gas introduction port of the gas path to the gas outlet is airtight,
    The third water release amount suppressing means comprises, from the upstream side, a water-repellent nonwoven fabric filter having a fiber diameter of 1 μm or more and 30 μm or less and a pressure loss of 20 Pa or more and 60 Pa or less, and a hydrophobic fiber having a fiber diameter of 70 nm or more and 200 nm or less. A double filter consisting of a nanofilter containing a soluble nanofiber and having a pressure loss of 20 Pa or more and 60 Pa or less, and the space between the double filters is at least 5 mm or more.
    The hypochlorous acid gas generator according to claim 2, characterized in that:
  6.  前記ガス放出口に装着された前記水分放出量抑制手段の上流面が、傾斜面をなし、
     前記上流面で滴となったミストが、前記傾斜面に沿って前記貯留槽に落下される、
    ことを特徴とする請求項3乃至請求項5のいずれか一項に記載の次亜塩素酸ガス発生装置。
    an upstream surface of the moisture release suppressing means attached to the gas outlet forms an inclined surface,
    the mist droplets on the upstream surface fall into the storage tank along the inclined surface;
    The hypochlorous acid gas generator according to any one of claims 3 to 5, characterized in that:
  7.  前記ガス放出口の外方に、気流を発生させるガス拡散手段が備えられ、
     前記ガス拡散手段が、前記ガス放出口から放出された次亜塩素酸ガスを拡散させる、
    ことを特徴とする請求項3乃至請求項5のいずれか一項に記載の次亜塩素酸ガス発生装置。
    A gas diffusion means for generating an airflow is provided outside the gas outlet,
    The gas diffusion means diffuses the hypochlorous acid gas released from the gas outlet,
    The hypochlorous acid gas generator according to any one of claims 3 to 5, characterized in that:
  8.  空調システムにおいて、
     気相状態の次亜塩素酸のみを発生させて室内に供給させる空調システムであって、
     請求項1の記載の次亜塩素酸ガス発生構造を空調経路に備え、
     気相状態となるミストと次亜塩素酸ガスのみを、室内への新鮮空気導入経路に導入させて供給する、
    ことを特徴とする空調システム。
    In the air conditioning system,
    An air conditioning system that generates and supplies only hypochlorous acid in a gaseous state to a room,
    Equipping an air conditioning route with the hypochlorous acid gas generating structure according to claim 1,
    Only the vapor phase mist and hypochlorous acid gas are introduced into the fresh air introduction route into the room and supplied.
    An air conditioning system characterized by:
  9.  空調域が複数の区画に分割された建物において、
     人が滞在する区画毎に、気相状態の次亜塩素酸のみを発生させる請求項8に記載の空調システムが備えられている、
    ことを特徴とする建物。
    In a building where the air conditioning area is divided into multiple compartments,
    The air conditioning system according to claim 8, which generates only hypochlorous acid in a gas phase state, is provided for each section where people stay,
    A building characterized by
PCT/JP2022/014784 2022-01-11 2022-03-28 Hypochlorous acid gas generation structure, hypochlorous acid gas generation device, air conditioning system, and building WO2023135829A1 (en)

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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000197689A (en) * 1998-11-04 2000-07-18 Okazaki Tatsuo Indoor sterilization and deodorization method by hypochlorous acid-containing aqueous solution and apparatus therefor
JP2007312988A (en) * 2006-05-25 2007-12-06 Sanyo Electric Co Ltd Air disinfecting device
JP2019154884A (en) * 2018-03-15 2019-09-19 株式会社グリーンウェル Sterilization/deodorization system using hypochlorite tablet
JP3224953U (en) * 2019-11-15 2020-01-30 Red株式会社 Dry sterilizer and deodorizer

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000197689A (en) * 1998-11-04 2000-07-18 Okazaki Tatsuo Indoor sterilization and deodorization method by hypochlorous acid-containing aqueous solution and apparatus therefor
JP2007312988A (en) * 2006-05-25 2007-12-06 Sanyo Electric Co Ltd Air disinfecting device
JP2019154884A (en) * 2018-03-15 2019-09-19 株式会社グリーンウェル Sterilization/deodorization system using hypochlorite tablet
JP3224953U (en) * 2019-11-15 2020-01-30 Red株式会社 Dry sterilizer and deodorizer

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