WO2015158254A1 - 用于产生负氧离子的方法和装置及用于净化空气的方法和装置 - Google Patents

用于产生负氧离子的方法和装置及用于净化空气的方法和装置 Download PDF

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Publication number
WO2015158254A1
WO2015158254A1 PCT/CN2015/076595 CN2015076595W WO2015158254A1 WO 2015158254 A1 WO2015158254 A1 WO 2015158254A1 CN 2015076595 W CN2015076595 W CN 2015076595W WO 2015158254 A1 WO2015158254 A1 WO 2015158254A1
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Prior art keywords
water
air
gas
oxygen ions
negative oxygen
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PCT/CN2015/076595
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English (en)
French (fr)
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刘晓岳
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刘晓岳
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Priority to EP15780021.0A priority Critical patent/EP3132807A4/en
Priority to US15/304,435 priority patent/US10722606B2/en
Publication of WO2015158254A1 publication Critical patent/WO2015158254A1/zh

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    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61L—METHODS 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
    • A61L9/00—Disinfection, sterilisation or deodorisation of air
    • A61L9/16—Disinfection, sterilisation or deodorisation of air using physical phenomena
    • A61L9/22—Ionisation
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61L—METHODS 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
    • A61L9/00—Disinfection, sterilisation or deodorisation of air
    • A61L9/14—Disinfection, sterilisation or deodorisation of air using sprayed or atomised substances including air-liquid contact processes
    • A61L9/145—Disinfection, sterilisation or deodorisation of air using sprayed or atomised substances including air-liquid contact processes air-liquid contact processes, e.g. scrubbing
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D49/00—Separating dispersed particles from gases, air or vapours by other methods
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/46—Removing components of defined structure
    • B01D53/72—Organic compounds not provided for in groups B01D53/48 - B01D53/70, e.g. hydrocarbons
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/76—Gas phase processes, e.g. by using aerosols
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24—HEATING; RANGES; VENTILATING
    • F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F3/00—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems
    • F24F3/12—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling
    • F24F3/14—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24—HEATING; RANGES; VENTILATING
    • F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F8/00—Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying
    • F24F8/30—Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying by ionisation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2251/00—Reactants
    • B01D2251/10—Oxidants
    • B01D2251/102—Oxygen
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2257/00—Components to be removed
    • B01D2257/70—Organic compounds not provided for in groups B01D2257/00 - B01D2257/602
    • B01D2257/702—Hydrocarbons
    • B01D2257/7027—Aromatic hydrocarbons
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2257/00—Components to be removed
    • B01D2257/70—Organic compounds not provided for in groups B01D2257/00 - B01D2257/602
    • B01D2257/708—Volatile organic compounds V.O.C.'s
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2258/00—Sources of waste gases
    • B01D2258/06—Polluted air

Definitions

  • the present invention relates to a method and apparatus for generating negative oxygen ions and a method and apparatus for purifying air.
  • the content of negative oxygen ions is one of the important indicators of the quality of air quality.
  • the United Nations stipulates that the standard for fresh air is 1000 to 1500 negative oxygen ions per cubic centimeter, while in the forest area up to 100,000 negative oxygen ions per cubic centimeter, while in Chinese cities there are generally only tens to hundreds of negative oxygen ions per cubic. In centimeters, many closed buildings will be as low as a dozen negative oxygen ions per cubic centimeter.
  • the common feature of the above air purification technology is that the membrane is used to trap the particles in the air.
  • the dust particles will quickly block the pores, the purification effect is reduced, and the filter screen needs to be replaced continuously. Consumables will greatly increase the cost of effective use.
  • the air containing negative oxygen ions after the reaction is separated from the water after the reaction, and the air containing negative oxygen ions after the reaction is released to a desired space.
  • the method for producing negative oxygen ions of the present invention can provide the following advantageous technical effects: a large amount of negative oxygen ions can be efficiently and inexpensively produced without generating any harmful substances such as ozone, nitrogen oxides and the like.
  • the volume ratio of water to air introduced is from 5:1000 to 50:1000.
  • the method for producing negative oxygen ions of the present invention can have the following advantageous technical effects: a large amount of negative oxygen ions can be generated more efficiently.
  • the relative movement speed of the introduced air and water in the gas-water reactor up to 20 m/sec or more is achieved by: paddle hitting at a speed of 50 to 500 rpm
  • the water in the gas-water reactor is formed into water droplets having a velocity of 20 m/sec or more to cause the water droplets to collide with the introduced air. Hit and rub.
  • the method for generating negative oxygen ions of the present invention can provide the following beneficial technical effects: the introduced air and water can be achieved in the gas-water reactor up to 20 m/sec or more in a simple and effective manner. The relative speed of movement, so that a large amount of negative oxygen ions can be generated efficiently and at low cost without generating any harmful substances such as ozone.
  • the relative movement speed of the introduced air and water in the gas-water reactor to a temperature of 20 m/sec or more is achieved by impinging and rubbing the water flow by an air flow having a velocity of 20 m/sec or more.
  • the method for generating negative oxygen ions of the present invention can provide the following beneficial technical effects: the introduced air and water can be achieved in the gas-water reactor up to 20 m/sec or more in a simple and effective manner. The relative speed of movement, so that a large amount of negative oxygen ions can be generated efficiently and at low cost without generating any harmful substances such as ozone.
  • the water stream is dispersed by a splash plate disposed in the gas water reactor prior to impacting and rubbing the water stream by an air flow having a velocity of 20 m/sec or more.
  • the method for producing negative oxygen ions of the present invention can provide the following advantageous technical effects: the water flow is sufficiently dispersed before being impacted and rubbed by the high-speed air stream, so that a large amount of negative oxygen ions can be generated more efficiently.
  • a device for generating negative oxygen ions comprising:
  • a gas-water reactor for introducing air and water, respectively, such that the introduced air and water reach a relative movement speed of 20 m/sec or more in the gas-water reactor to react in the gas-water reaction Reacts within the device to produce negative oxygen ions;
  • gas-water separator disposed downstream of the gas-water reactor, the gas-water separator is configured to separate air containing negative oxygen ions after the reaction from water after the reaction, and release the air containing negative oxygen ions after the reaction to The space required.
  • the apparatus for generating negative oxygen ions of the present invention can provide the following advantageous technical effects: a large amount of negative oxygen ions can be efficiently and inexpensively produced without generating any harmful substances such as ozone, nitrogen oxides and the like.
  • the volume ratio of water to air introduced is from 5:1000 to 50:1000.
  • the apparatus for generating negative oxygen ions of the present invention can provide the following advantageous technical effects: a large amount of negative oxygen ions can be generated more efficiently.
  • the gas water reactor comprises a paddle for hitting water in the gas water reactor at a rotational speed of 50 to 500 rpm to form a velocity of 20 m/sec.
  • the above water droplets cause the water droplets to collide and rub against the introduced air.
  • the apparatus for generating negative oxygen ions of the present invention can provide the following beneficial technical effects: the introduced air and water can be achieved in the gas-water reactor up to 20 m/sec or more in a simple and effective manner. The relative speed of movement, so that a large amount of negative oxygen ions can be generated efficiently and at low cost without generating any harmful substances such as ozone.
  • the gas-water reactor includes an intake portion for causing the air flow to reach a speed of 20 m/sec or more to impact and rub the water flow.
  • the apparatus for generating negative oxygen ions of the present invention can provide the following beneficial technical effects: the introduced air and water can be achieved in the gas-water reactor up to 20 m/sec or more in a simple and effective manner. The relative speed of movement, so that a large amount of negative oxygen ions can be generated efficiently and at low cost without generating any harmful substances such as ozone.
  • the gas water reactor further includes a splash plate disposed in the gas water reactor for dispersing the water stream before being impacted and rubbed by the air stream.
  • the apparatus for generating negative oxygen ions of the present invention can provide the following advantageous technical effects: the water flow is sufficiently dispersed before being impacted and rubbed by the high-speed air stream, so that a large amount of negative oxygen ions can be generated more efficiently.
  • Another object of the present invention is to overcome the above-discussed deficiencies of the prior art methods and apparatus for purifying air, and to provide a method and apparatus for purifying air that can purify air efficiently and at low cost without generating any ozone such as ozone Hazardous substances, and long-term maintenance-free.
  • the above object of the present invention is achieved by a method for purifying air, the method for purifying air comprising:
  • the purified air containing negative oxygen ions after the reaction is separated from the water after the reaction, and the reaction is contained
  • the purified air of negative oxygen ions is released to the required space.
  • the method for purifying air of the present invention can achieve the following beneficial technical effects: high-efficiency and low-cost purification of air (suitable for removing particles of various concentrations and various particle sizes) without generating ozone, nitrogen, etc. Any harmful substances such as oxides, and long-term maintenance-free.
  • the volume ratio of water to air introduced is from 5:1000 to 50:1000.
  • the method for purifying air of the present invention can provide the following advantageous technical effects: a large amount of negative oxygen ions can be generated more efficiently and the air can be purified.
  • the relative movement speed of the introduced air and water in the gas-water reactor up to 20 m/sec or more is achieved by: paddle hitting at a speed of 50 to 500 rpm
  • the water in the gas-water reactor is formed into water droplets having a velocity of 20 m/sec or more so that the water droplets collide with the introduced air and rub.
  • the method for purifying air of the present invention can provide the following beneficial technical effects: the relative introduction of air and water in the gas-water reactor can reach a relative position of 20 m/sec or more in a simple and effective manner. The speed of movement, so that a large amount of negative oxygen ions can be efficiently and cost-effectively produced and the air is purified without generating any harmful substances such as ozone.
  • the relative movement speed of the introduced air and water in the gas-water reactor to a temperature of 20 m/sec or more is achieved by impinging and rubbing the water flow by an air flow having a velocity of 20 m/sec or more.
  • the method for purifying air of the present invention can provide the following beneficial technical effects: the relative introduction of air and water in the gas-water reactor can reach a relative position of 20 m/sec or more in a simple and effective manner. The speed of movement, so that a large amount of negative oxygen ions can be efficiently and cost-effectively produced and the air is purified without generating any harmful substances such as ozone.
  • the water stream is dispersed by a splash plate disposed in the gas water reactor prior to impacting and rubbing the water stream by an air flow having a velocity of 20 m/sec or more.
  • the method for purifying air of the present invention can provide the following advantageous technical effects: the water flow is sufficiently dispersed before being impacted and rubbed by the high-speed air stream, so that a large amount of negative oxygen ions can be generated more efficiently and the air can be purified.
  • a further object of the present invention is also achieved by a device for purifying air, the device for purifying air comprising:
  • a gas-water reactor for introducing air and water, respectively, such that the introduced air and water reach a relative movement speed of 20 m/sec or more in the gas-water reactor to react in the gas-water reaction a reaction occurs within the device to generate negative oxygen ions and to purify the air;
  • gas-water separator disposed downstream of the gas-water reactor, the gas-water separator for separating the purified air containing negative oxygen ions after the reaction from the water after the reaction, and purifying the air containing negative oxygen ions after the reaction Release to the required space.
  • the device for purifying air of the present invention can have the following beneficial technical effects: high-efficiency and low-cost purification of air (suitable for removing particles of various concentrations and various particle sizes) without generating ozone, nitrogen, etc. Any harmful substances such as oxides, and long-term maintenance-free.
  • the volume ratio of water to air introduced is from 5:1000 to 50:1000.
  • the apparatus for purifying air of the present invention can provide the following advantageous technical effects: it can purify air efficiently and at low cost without generating any harmful substances such as ozone, and is long-lasting and maintenance-free.
  • the gas water reactor comprises a paddle for hitting water in the gas water reactor at a rotational speed of 50 to 500 rpm to form a velocity of 20 m/sec.
  • the above water droplets cause the water droplets to collide and rub against the introduced air.
  • the apparatus for purifying air of the present invention can provide the following advantageous technical effects: the relative introduction of air and water in the gas-water reactor can reach a relative position of 20 m/sec or more in a simple and effective manner. The speed of movement, so that a large amount of negative oxygen ions can be efficiently and cost-effectively produced and the air is purified without generating any harmful substances such as ozone.
  • the gas-water reactor includes an intake portion for causing the air flow to reach a speed of 20 m/sec or more to impact and rub the water flow.
  • the apparatus for purifying air of the present invention can provide the following advantageous technical effects: the relative introduction of air and water in the gas-water reactor can reach a relative position of 20 m/sec or more in a simple and effective manner. The speed of movement, so that a large amount of negative oxygen ions can be efficiently and cost-effectively produced and the air is purified without generating any harmful substances such as ozone.
  • the gas water reactor further includes a splash plate disposed in the gas water reactor for dispersing the water stream before being impacted and rubbed by the air stream.
  • the device for purifying air of the present invention can have the following beneficial technical effects. If the water flow is fully dispersed before being impacted and rubbed by the high-speed airflow, it can generate a large amount of negative oxygen ions and purify the air more efficiently.
  • FIG. 1 is a schematic illustration of a method and apparatus for producing negative oxygen ions or for purifying air in accordance with the present invention.
  • Figure 2 (a) is a schematic illustration of a method and apparatus for producing negative oxygen ions or for purifying air in accordance with a first embodiment of the present invention.
  • Fig. 2(b) is a cross-sectional view taken along line A-A of Fig. 2(a).
  • FIG. 3 is a schematic diagram of a method and apparatus for generating negative oxygen ions or for purifying air in accordance with a second embodiment of the present invention.
  • FIG. 4 is a schematic diagram of a method and apparatus for generating negative oxygen ions or for purifying air in accordance with a third embodiment of the present invention.
  • Figure 5 (a) is a schematic plan view of a method and apparatus for generating negative oxygen ions or for purifying air in accordance with a fourth embodiment of the present invention.
  • Figure 5 (b) is a schematic side view of a method and apparatus for generating negative oxygen ions or for purifying air in accordance with a fourth embodiment of the present invention.
  • Figure 1 shows a schematic diagram of a method and apparatus for producing negative oxygen ions or for purifying air in accordance with the present invention.
  • methods for generating negative oxygen ions or for purifying air include:
  • the purified air containing negative oxygen ions after the reaction is separated from the water after the reaction, and the purified air containing negative oxygen ions after the reaction is released to a desired space.
  • the means for generating negative oxygen ions or for purifying air includes:
  • a gas-water reactor for introducing air and water, respectively, so that the introduced air and water react in the gas-water reactor to a relative movement speed of 20 m/sec or more in the gas-water reactor, thereby Produces negative oxygen ions and purifies the air;
  • gas-water separator disposed downstream of the gas-water reactor, wherein the gas-water separator is used to separate the purified air containing negative oxygen ions from the water after the reaction, and release the purified air containing negative oxygen ions after the reaction to the desired space.
  • Negative oxygen ions and water mist enter the gas water separator, water is returned to the bottom of the gas water reactor, and the purified air containing negative oxygen ions is released from the gas outlet of the gas water separator. Need space.
  • the main components of air are nitrogen, oxygen, and carbon dioxide.
  • the contents are 78%, 21%, and 0.03%, respectively.
  • Nitrogen has no affinity for electrons, so it can only form negative ions of oxygen and carbon dioxide.
  • the binding efficiency of carbon dioxide molecules, oxygen molecules and negative charges is basically the same, but the concentration of carbon dioxide in the air is only 1/700 of that of oxygen, so the negative charge is basically captured by oxygen and becomes a negative oxygen ion.
  • water water mist and water vapor
  • negative oxygen ions can effectively remove particles of various particle sizes in the air and purify the air.
  • the violent relative motion of the water vapor in the gas-water reactor has a strong purification effect on large particles (above PM2.5) in the air, and a large amount of negative oxygen ions are generated to the small particles in the air (PM2. 5) It has a strong purifying effect.
  • PM2.5 Small particles
  • the positively charged particles are mainly organic carbon molecules, such as formaldehyde, benzene, etc., and negative oxygen ions can make them neutralize, aggregate and separate.
  • Electroneutral particles mainly viruses and bacteria, negatively charged by negative oxygen ions can alter microbial genetic material and cause apoptosis.
  • the negatively charged particles are mainly sulfate, hydrochloride, nitrate, chloride, etc., and are hydrophilic and can be removed by water mist.
  • the introduced air and water react in the gas-water reactor at a relative speed of movement of up to 40 m/sec or more in the gas-water reactor.
  • the gas-water reaction time in the gas-water reactor is less than 1 second.
  • the gas water separator comprises a centrifugal separator or a swash plate inertial separator.
  • the centrifugal separator has an adjustable gyro angle. In this way, the gas-water separation (dehydration) efficiency can be adjusted.
  • a series of devices for generating negative oxygen ions or for purifying air can be produced, suitable for use in different volumes of indoor or in-vehicle or other enclosed environments.
  • the present invention can provide a method and apparatus for generating negative oxygen ions which can efficiently generate a large amount of negative oxygen ions without generating any harmful substances such as ozone.
  • the present invention can also provide a method and apparatus for purifying air capable of purifying air at high cost and low cost (regardless of the original concentration and particle size of the particulate matter, and not limited to the working time of the apparatus) without generating ozone, nitrogen, etc. Any harmful substances such as oxides, and long-term maintenance-free.
  • the present invention also has a function of adjusting the humidity of the air and adjusting the temperature of the air.
  • Figure 2 (a) is a schematic illustration of a method and apparatus for producing negative oxygen ions or for purifying air in accordance with a first embodiment of the present invention.
  • Fig. 2(b) is a cross-sectional view taken along line A-A of Fig. 2(a).
  • a gas-water reactor 101 for introducing air and water, respectively, so that the introduced air and water reach a relative movement speed of 20 m/sec or more in the gas-water reactor and occur in the gas-water reactor Reacting to generate negative oxygen ions and purify the air;
  • the gas-water reactor 101 of the first embodiment of the present invention is, for example, a straight-tank gas-water reactor placed horizontally.
  • a straight barrel gas water reactor has a diameter of 20 cm and a length of 80 cm.
  • the apparatus for generating negative oxygen ions or for purifying air according to the first embodiment of the present invention may further include an induced draft fan 103, which is advantageously disposed downstream of the gas water separator 102 for more effective after the reaction
  • the purified air containing negative oxygen ions is released to the required space.
  • a blower located at another position can be provided instead of the induced draft fan, and the purified air containing negative oxygen ions after the reaction can be more effectively released to the required space.
  • the apparatus for generating negative oxygen ions or for purifying air of the first embodiment of the present invention may further include a paddle shaft 104 and one or more sets of paddles 105.
  • the paddles can hit the water in the gas-water reactor 101 at a rotational speed of 50 to 500 rpm to form water droplets having a velocity of 20 m/sec or more, so that the water droplets collide with the introduced air and rub.
  • the apparatus for generating negative oxygen ions or for purifying air according to the first embodiment of the present invention may also preferably include an intake port, an air outlet, a water level controller, a water inlet, a water pump, an electric motor, a speed reducer, and the like.
  • the gas-water reactor 101 has a 5*10 cm air inlet directly above the left side of the barrel, and a 5*10 cm air outlet is directly above the right side of the gas-water reactor 101.
  • the paddle shaft 104 is 85 cm long and runs through the barrel to seal the bushing to the barrel.
  • the end of the paddle shaft 104 is connected to a speed reducer (not shown) outside the gas-water reactor 101, and is driven by a motor 106 connected to the speed reducer.
  • a speed reducer not shown
  • 20 sets of four-bladed paddles 105 are provided on the paddle shaft 104.
  • the blade 105 is 6 cm long and 1 cm wide and is a rectangular flat design with a thickness of 3 mm.
  • the spacing of each set of blades 105 is 2 cm.
  • the water depth is controlled to 6 cm by the water level controller, and the gas water separator 102 is connected to the air outlet by the gas water separator 102 on the upper right side of the barrel.
  • the gas water separator 102 is preferably a multi-tube cyclone mist eliminator.
  • the bottom of the gas-water separator 102 is provided with a drain port, and the separated water is returned to the gas-water reactor 101.
  • the motor 106 drives the paddle 105 to rotate at a speed of 120 revolutions per second, hitting the liquid surface at a high speed, generating a large amount of water droplets, accelerating the water droplets to a maximum speed of 43 meters per second, and accelerating high-speed cutting of water droplets after the acceleration, Rubbing the air, the water loses electrons, the lost electrons become space free electrons, and the space free electrons combine with oxygen to form a large amount of negative oxygen ions.
  • the negative oxygen ions and the water mist enter the gas-water separator 102 under the action of the induced draft fan 103, and the water is separated and returned to the bottom of the gas-water reactor 101, and the air containing the negative oxygen ions is discharged from the gas outlet of the gas-water separator 102.
  • the inner wall of the gas-water separator is smooth and has no uneven structure. In this way, it is ensured that the water droplets are always maintained at a speed of 20 m/sec or more.
  • the outer surface of the blade is rough. In this way, it is ensured that the water droplets can be effectively collected when the blade hits the water surface.
  • the cross section of the blade is generally rectangular. In this way, it is further ensured that the water droplets are effectively collected when the blade hits the water surface, and the water droplets are provided at a speed of 20 m/sec or more.
  • Devices for generating negative oxygen ions or for purifying air in various closed spaces can be achieved by adjusting the power and size of the equipment.
  • FIG. 3 is a schematic diagram of a method and apparatus for generating negative oxygen ions or for purifying air in accordance with a second embodiment of the present invention.
  • a gas-water reactor 201 for introducing air and water, respectively, so that the introduced air and water reach a relative movement speed of 20 m/sec or more in the gas-water reactor and occur in the gas-water reactor Reacting to generate negative oxygen ions and purify the air;
  • the gas-water reactor 201 of the second embodiment of the present invention is, for example, a vertically placed straight-tank gas-water reactor.
  • a straight barrel gas water reactor has a diameter of 20 cm and a height of 80 cm.
  • the apparatus for generating negative oxygen ions or for purifying air according to the second embodiment of the present invention may further include an induced draft fan 203, which is advantageously disposed downstream of the gas water separator 202 for more effective after the reaction
  • the purified air containing negative oxygen ions is released to the required space.
  • a blower located at another position can be provided instead of the induced draft fan, and the purified air containing negative oxygen ions after the reaction can be more effectively released to the required space.
  • the apparatus for generating negative oxygen ions or for purifying air of the second embodiment of the present invention may further include a paddle shaft 204 and one or more sets of paddles 205.
  • the blade can be hit in the gas water at a speed of 50 to 500 rpm.
  • the water sprinkled from the water sprayer 208 in the reactor 201 forms water droplets having a speed of 20 m/sec or more to cause water droplets to collide with and rub against the introduced air.
  • the apparatus for generating negative oxygen ions or for purifying air according to the second embodiment of the present invention may preferably further include an intake port, an air outlet, a water inlet, a water pump 207, an electric motor 206, a speed reducer, and the like.
  • a gas jet reactor 201 is provided with a 5*10 cm outlet port on the top side, and two 9 cm diameter sprinklers 208 are disposed 10 cm below the gas outlet.
  • the height of the paddle shaft 204 is 40 cm, the height of the four sets of blades on the paddle shaft is 2 cm, and the length is 9.6 cm.
  • the four sets of blades are arranged in an angularly staggered manner from 5 to 20 cm below the sprinkler 208. Interval.
  • the gas-water reactor 201 has a 5*10 cm inlet port on the wall 20 cm from the bottom.
  • the lower part of the gas-water reactor 201 is an open water tank with a liquid level of 10 cm.
  • water pump 207 sprays water from sprinkler 208 at a flow rate of 0.2 liters per second from the bottom tank of gas-water reactor 201.
  • the four sets of blades are driven by the motor at the same speed of 120 rpm, and the sprayed water body is hit at high speed to accelerate the water droplets to a maximum speed of 72 meters per second.
  • the accelerated water droplets cut at high speed and rub the air.
  • Water loses electrons, and lost electrons become space free electrons. Space free electrons combine with oxygen to form a large amount of negative oxygen ions.
  • the air carrying the water mist and the negative oxygen ions enters the gas water separator 202 from the air outlet, and the water is separated and returned to the water tank.
  • the air containing negative oxygen ions is discharged from the gas outlet of the gas water separator 202.
  • Devices for generating negative oxygen ions or for purifying air in various closed spaces can be achieved by adjusting the power and size of the equipment.
  • FIG. 4 is a schematic diagram of a method and apparatus for generating negative oxygen ions or for purifying air in accordance with a third embodiment of the present invention.
  • a gas-water reactor 301 for introducing air and water, respectively, so that the introduced air and water reach a relative movement speed of 20 m/sec or more in the gas-water reactor and occur in the gas-water reactor Reacting to generate negative oxygen ions and purify the air;
  • the gas-water reactor 301 of the third embodiment of the present invention is, for example, a long cubic gas-water reactor.
  • the gas-water reactor 301 is 30 cm long, 20 cm wide, and 60 cm high.
  • the apparatus for generating negative oxygen ions or for purifying air according to the third embodiment of the present invention may preferably further include an intake port, an air outlet, a water spout pipe 308, a water pump 307, and the like.
  • the upper surface of the gas-water reactor 301 is open, and a vertical plate 309 is disposed on the upper portion, and the casing is divided into two portions having lengths of 10 cm and 20 cm, respectively, the narrow side is an air inlet, and the wide side is an air outlet.
  • the riser 309 is flush with the upper surface of the cabinet and is 20 cm from the bottom of the cabinet.
  • the bottom of the tank is a water tank with a water depth of 15 cm and is preferably provided with a water level controller connected to the water source.
  • two spray pipes 308 having a cross-sectional area of 1 mm 2 are provided, 15 cm from the top of the tank.
  • the water spray pipe 308 is connected to the water tank at the bottom of the tank through a water pump 307.
  • the pump 307 has a pressure of 0.4 MPa and a flow rate of 1 liter per second.
  • a gas-water separator 302 is disposed at the upper portion of the wide side.
  • the gas-water separator 302 is, for example, a swash plate type inertia dehydrator having a tilt angle of 55 degrees.
  • the air outlet above the cabinet is connected to the induced draft fan.
  • the water pump 307 sprays water through the water spray pipe 308 at a pressure of 0.4 MPa, and impinges on the riser 309.
  • the water flow cuts at high speed, rubs the air, the water loses electrons, and the lost electrons become space free electrons, and the space is free.
  • the combination of electrons and oxygen forms a large amount of negative oxygen ions.
  • the negative oxygen ions and the water mist enter the right gas water separator 302 (the swash plate type inertia dehydrator) under the action of the induced draft fan, and the water is separated and returned to the bottom of the gas water reactor 301, and the air containing the negative oxygen ions is taken from the induced draft fan.
  • the air outlet is discharged.
  • Devices for generating negative oxygen ions or for purifying air in various closed spaces can be achieved by adjusting the power and size of the equipment.
  • Figure 5 (a) is a schematic plan view of a method and apparatus for generating negative oxygen ions or for purifying air according to a fourth embodiment of the present invention
  • Figure 5 (b) is a fourth embodiment of the present invention for generating negative oxygen
  • a gas-water reactor 401 for separately introducing air and water to cause the introduced air and water to reach a relative movement speed of 20 m/sec or more in the gas-water reactor to occur in the gas-water reactor Reacting to generate negative oxygen ions and purify the air;
  • the air is sucked into the intake pipe 411 (also referred to as "intake portion") from the intake port having a cross-sectional area of 200 cm 2 by the fan, and the air velocity is 5 m/s.
  • the pipe section is reduced to make the air velocity. Accelerate to 40 m/s (of course, the air velocity of 40 m/s here is only an example, and in the principle of the present invention, as long as the air flow rate of 20 m/sec or more is used), the gas-water reactor 401 is entered.
  • water is sprayed into the gas-water reactor 401 by the water pump and the water spray pipe 408 before the inlet 412, and the water is flushed toward the splash plate 410 in front of the inlet 412, and then repeatedly cut and rubbed by the high-speed airflow, and the water loses electrons. Lost electrons become space free electrons, and space free electrons combine with oxygen to form a large amount of negative oxygen ions. At the same time, a large amount of water mist and water vapor are formed in the gas-water reactor 401.
  • the negative oxygen ions and the water mist enter the gas-water separator 402 on the right side, for example, under the action of the induced draft fan 403. Under the action of centrifugal force, various particulate matter is finally separated along with the water body, and flows into the water tank to precipitate and complete the removal.
  • the air only carries negative oxygen ions and part of the water vapor back into the room, and the negative oxygen ions diffuse indoors, and the PM2.5 in the room continues to be removed.
  • the volume ratio of water to air introduced is from 5:1000 to 50:1000.
  • the air flow at a speed of 20 m/sec or more is generated by the air passage reducer.
  • the method and the device can achieve a single removal rate of more than 95% for each particle size of the air flowing through the gas-water reactor.
  • Devices for generating negative oxygen ions or for purifying air in various closed spaces can be achieved by adjusting the power and size of the equipment.
  • the scope of protection of the present invention is It is not limited to the specific configurations of the above-listed methods for generating negative oxygen ions or for purifying air, but other configurations for generating negative oxygen ions or for purifying air may be employed.
  • Gas method and device According to the principles of the present invention, the method for producing negative oxygen ions or for purifying air includes the steps of introducing air and water into the gas water reactor separately, so that the introduced air and water are in the gas water reactor.
  • the apparatus for generating negative oxygen ions or for purifying air includes a gas water reactor and a gas water separator as follows: a gas water reactor for introducing air and water, respectively, for introduction The air and water reach a relative motion speed of 20 m / sec or more in the gas-water reactor and react in the gas-water reactor to generate negative oxygen ions and purify the air; the gas-water separator is set in the gas-water reaction Downstream of the device, a gas-water separator is used to separate the purified air containing negative oxygen ions from the water after the reaction, and to release the purified air containing negative oxygen ions into the required space after the reaction.
  • the present invention In addition to the function of generating negative oxygen ions and purifying air, it is preferred that the present invention also has a function of temperature regulation and humidity adjustment, that is, the present invention may be an air conditioning apparatus operating on a new principle.
  • the method for generating negative oxygen ions or for purifying air further comprises adjusting the temperature of the water prior to introducing the water into the gas water reactor to adjust the temperature of the released air.
  • the means for generating negative oxygen ions or for purifying air further comprises a water temperature regulator for regulating the temperature of the water prior to introducing the water into the gas water reactor to adjust the released air. temperature.
  • the principle of the present invention for adjusting the temperature of the air is as follows: as long as the temperature of the water introduced into the gas-water reactor is adjusted, the temperature of the released air can be adjusted, because in the gas-water reactor, the water body is thoroughly mixed with the air, and the two directly exchange heat. Thereby rapidly changing the temperature of the released air.
  • the invention can also adjust the humidity of the air.
  • the principle is as follows: in the drying season, since the output airflow of the present invention contains water vapor, the room can be humidified; in the high-humidity season, the gas-water reactor of the present invention draws in indoor high-humidity air. A part of the water vapor is condensed and liquefied and separated from the air in the dehydrator, and no longer enters the room, reducing the indoor humidity.
  • the present invention can be used as a new principle air conditioner, and has three meanings:
  • the conventional air conditioner is indirectly heating or cooling air, and the invention is to make water and air directly contact for heat exchange, and the efficiency is greatly improved.
  • the air output by the traditional air conditioner is dry air, the human body will feel uncomfortable, and the present invention can Maintain a livable relative humidity environment indoors.
  • the conventional air conditioner cannot remove PM2.5 in the air and harmful gases such as formaldehyde, nor can it generate negative oxygen ions to improve the air quality.
  • the present invention can simultaneously achieve the above functions.

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Abstract

用于产生负氧离子的方法和装置及用于净化空气的方法和装置。所述用于产生负氧离子的方法包括：将空气和水分别引入气水反应器，以使引入的空气和水在所述气水反应器内达到20米/秒以上的相对运动速度而在所述气水反应器内发生反应，从而产生负氧离子；以及将反应之后含负氧离子的空气与反应之后的水分离，并将反应之后含负氧离子的空气释放到所需空间。所述方法和装置能高效低成本地产生大量负氧离子和净化空气而不产生诸如臭氧、氮氧化物等的任何有害物质，并且长效免维护。

Description

用于产生负氧离子的方法和装置及用于净化空气的方法和装置
本申请要求于2014年4月17日提交的、申请号为201410155480.9的中国专利申请的优先权，在此以参见的方式引入该申请的全部内容。
技术领域
本发明涉及用于产生负氧离子的方法和装置及用于净化空气的方法和装置。
背景技术
负氧离子的含量是空气质量优劣的重要标志之一。联合国规定清新空气的标准是1000到1500个负氧离子/立方厘米，而在森林地区高达10万个负氧离子/立方厘米，而中国城市中一般只有几十到几百个负氧离子/立方厘米，很多封闭楼宇内更会低至十几个负氧离子/立方厘米。
目前产生负氧离子的技术多数是通过放电产生空间自由电子，电子再与氧气结合形成负氧离子，但这时也产生臭氧和氮氧化物等有害物质，成为这种干式负氧发生器推广应用的一个障碍。
目前国际上有一种富勒烯负氧离子释放剂，但因价格偏高尚未得到广泛应用。
因此，希望能有一种用于产生负氧离子的方法和装置，其能高效低成本地产生大量负氧离子而不产生诸如臭氧的任何有害物质。
此外，随着雾霾现象的加重，近年来对空气净化器的需求日益增加。目前空气净化器大多数是过滤式：即将空气通过风机送到过滤器上，经过各种不同功能的滤网，分别达到滤除粗、中、细颗粒物的效果；更进一步的是具有物理捕集和化学分解功能的滤网：矿晶膜、光触媒分解膜、HEPA膜等等。
以上空气净化技术的共同特点是用滤膜捕集空气中的颗粒物，当工作时间较长或环境恶劣时，尘粒很快会堵塞孔隙，净化效果下降，需不断更换滤网等 耗材，将大大提高有效使用成本。
还有一些采用高压静电除尘的方法來治理空气中的颗粒物,其效率较低而且会产生臭氧等有害物质。
近年来国外兴起用等离子体或净离子流净化器，可有效去除PM2.5但造价过高难以普及。
因此，还希望能有一种用于净化空气的方法和装置，其能高效低成本地净化空气而不产生诸如臭氧的任何有害物质，且长效免维护，无需更换滤网等耗材。
发明内容
本发明的一目的是克服现有技术用于产生负氧离子的方法和装置的上述缺陷，提供一种用于产生负氧离子的方法和装置，其能高效低成本地产生大量负氧离子而不产生诸如臭氧的任何有害物质。
本发明的以上目的通过一种用于产生负氧离子的方法来实现，所述用于产生负氧离子的方法包括：
将空气和水分别引入气水反应器，以使引入的空气和水在所述气水反应器内达到20米/秒以上的相对运动速度而在所述气水反应器内发生反应，从而产生负氧离子；以及
将反应之后含负氧离子的空气与反应之后的水分离，并将反应之后含负氧离子的空气释放到所需空间。
根据上述技术方案，本发明的用于产生负氧离子的方法能起到以下有益技术效果：能高效低成本地产生大量负氧离子而不产生诸如臭氧、氮氧化物等的任何有害物质。
较佳的是，引入的水和空气的体积比为5:1000至50:1000。
根据上述技术方案，本发明的用于产生负氧离子的方法能起到以下有益技术效果：能更高效地产生大量负氧离子。
较佳的是，引入的空气和水在所述气水反应器内达到20米/秒以上的相对运动速度通过以下方式来实现：由转速为50至500转/分的桨叶击打在所述气水反应器内的水，形成速度为20米/秒以上的水滴，以使水滴与引入的空气碰 撞、摩擦。
根据上述技术方案，本发明的用于产生负氧离子的方法能起到以下有益技术效果：能以简单有效的方式实现引入的空气和水在所述气水反应器内达到20米/秒以上的相对运动速度，从而能高效低成本地产生大量负氧离子而不产生诸如臭氧的任何有害物质。
较佳的是，引入的空气和水在所述气水反应器内达到20米/秒以上的相对运动速度通过以下方式来实现：由速度为20米/秒以上的空气流冲击、摩擦水流。
根据上述技术方案，本发明的用于产生负氧离子的方法能起到以下有益技术效果：能以简单有效的方式实现引入的空气和水在所述气水反应器内达到20米/秒以上的相对运动速度，从而能高效低成本地产生大量负氧离子而不产生诸如臭氧的任何有害物质。
较佳的是，在由速度为20米/秒以上的空气流冲击、摩擦水流之前，使水流被设置在所述气水反应器内的溅板分散。
根据上述技术方案，本发明的用于产生负氧离子的方法能起到以下有益技术效果：使水流在被高速气流冲击、摩擦之前充分散开，从而能更高效地产生大量负氧离子。
本发明的以上目的还通过一种用于产生负氧离子的装置来实现，所述用于产生负氧离子的装置包括：
气水反应器，所述气水反应器用于分别引入空气和水，以使引入的空气和水在所述气水反应器内达到20米/秒以上的相对运动速度而在所述气水反应器内发生反应，从而产生负氧离子；以及
设置在所述气水反应器下游的气水分离器，所述气水分离器用于将反应之后含负氧离子的空气与反应之后的水分离，并将反应之后含负氧离子的空气释放到所需空间。
根据上述技术方案，本发明的用于产生负氧离子的装置能起到以下有益技术效果：能高效低成本地产生大量负氧离子而不产生诸如臭氧、氮氧化物等的任何有害物质。
较佳的是，引入的水和空气的体积比为5:1000至50:1000。
根据上述技术方案，本发明的用于产生负氧离子的装置能起到以下有益技术效果：能更高效地产生大量负氧离子。
较佳的是，所述气水反应器包括桨叶，所述桨叶用于以50至500转/分的转速击打在所述气水反应器内的水，形成速度为20米/秒以上的水滴，以使水滴与引入的空气碰撞、摩擦。
根据上述技术方案，本发明的用于产生负氧离子的装置能起到以下有益技术效果：能以简单有效的方式实现引入的空气和水在所述气水反应器内达到20米/秒以上的相对运动速度，从而能高效低成本地产生大量负氧离子而不产生诸如臭氧的任何有害物质。
较佳的是，所述气水反应器包括进气部，所述进气部用于使空气流达到20米/秒以上的速度，以冲击、摩擦水流。
根据上述技术方案，本发明的用于产生负氧离子的装置能起到以下有益技术效果：能以简单有效的方式实现引入的空气和水在所述气水反应器内达到20米/秒以上的相对运动速度，从而能高效低成本地产生大量负氧离子而不产生诸如臭氧的任何有害物质。
较佳的是，所述气水反应器还包括溅板，所述溅板设置在所述气水反应器内以用于使水流在被空气流冲击、摩擦之前被分散。
根据上述技术方案，本发明的用于产生负氧离子的装置能起到以下有益技术效果：使水流在被高速气流冲击、摩擦之前充分散开，从而能更高效地产生大量负氧离子。
本发明的另一目的是克服现有技术用于净化空气的方法和装置的上述缺陷，提供一种用于净化空气的方法和装置，其能高效低成本地净化空气而不产生诸如臭氧的任何有害物质，且长效免维护。
本发明的以上目的通过一种用于净化空气的方法来实现，所述用于净化空气的方法包括：
将空气和水分别引入气水反应器，以使引入的空气和水在所述气水反应器内达到20米/秒以上的相对运动速度而在所述气水反应器内发生反应，从而产生负氧离子并使空气被净化；以及
将反应之后含负氧离子的净化空气与反应之后的水分离，并将反应之后含 负氧离子的净化空气释放到所需空间。
根据上述技术方案，本发明的用于净化空气的方法能起到以下有益技术效果：能高效低成本地净化空气(适用于清除各种浓度及各种粒径颗粒物)而不产生诸如臭氧、氮氧化物等的任何有害物质，且长效免维护。
较佳的是，引入的水和空气的体积比为5:1000至50:1000。
根据上述技术方案，本发明的用于净化空气的方法能起到以下有益技术效果：能更高效地产生大量负氧离子并净化空气。
较佳的是，引入的空气和水在所述气水反应器内达到20米/秒以上的相对运动速度通过以下方式来实现：由转速为50至500转/分的桨叶击打在所述气水反应器内的水，形成速度为20米/秒以上的水滴，以使水滴与引入的空气碰撞、摩擦。
根据上述技术方案，本发明的用于净化空气的方法能起到以下有益技术效果：能以简单有效的方式实现引入的空气和水在所述气水反应器内达到20米/秒以上的相对运动速度，从而能高效低成本地产生大量负氧离子并净化空气而不产生诸如臭氧的任何有害物质。
较佳的是，引入的空气和水在所述气水反应器内达到20米/秒以上的相对运动速度通过以下方式来实现：由速度为20米/秒以上的空气流冲击、摩擦水流。
根据上述技术方案，本发明的用于净化空气的方法能起到以下有益技术效果：能以简单有效的方式实现引入的空气和水在所述气水反应器内达到20米/秒以上的相对运动速度，从而能高效低成本地产生大量负氧离子并净化空气而不产生诸如臭氧的任何有害物质。
较佳的是，在由速度为20米/秒以上的空气流冲击、摩擦水流之前，使水流被设置在所述气水反应器内的溅板分散。
根据上述技术方案，本发明的用于净化空气的方法能起到以下有益技术效果：使水流在被高速气流冲击、摩擦之前充分散开，从而能更高效地产生大量负氧离子并净化空气。
本发明的以上另一目的还通过一种用于净化空气的装置来实现，所述用于净化空气的装置包括：
气水反应器，所述气水反应器用于分别引入空气和水，以使引入的空气和水在所述气水反应器内达到20米/秒以上的相对运动速度而在所述气水反应器内发生反应，从而产生负氧离子并使空气被净化；以及
设置在所述气水反应器下游的气水分离器，所述气水分离器用于将反应之后含负氧离子的净化空气与反应之后的水分离，并将反应之后含负氧离子的净化空气释放到所需空间。
根据上述技术方案，本发明的用于净化空气的装置能起到以下有益技术效果：能高效低成本地净化空气(适用于清除各种浓度及各种粒径颗粒物)而不产生诸如臭氧、氮氧化物等的任何有害物质，且长效免维护。
较佳的是，引入的水和空气的体积比为5:1000至50:1000。
根据上述技术方案，本发明的用于净化空气的装置能起到以下有益技术效果：能高效低成本地净化空气而不产生诸如臭氧的任何有害物质，且长效免维护。
较佳的是，所述气水反应器包括桨叶，所述桨叶用于以50至500转/分的转速击打在所述气水反应器内的水，形成速度为20米/秒以上的水滴，以使水滴与引入的空气碰撞、摩擦。
根据上述技术方案，本发明的用于净化空气的装置能起到以下有益技术效果：能以简单有效的方式实现引入的空气和水在所述气水反应器内达到20米/秒以上的相对运动速度，从而能高效低成本地产生大量负氧离子并净化空气而不产生诸如臭氧的任何有害物质。
较佳的是，所述气水反应器包括进气部，所述进气部用于使空气流达到20米/秒以上的速度，以冲击、摩擦水流。
根据上述技术方案，本发明的用于净化空气的装置能起到以下有益技术效果：能以简单有效的方式实现引入的空气和水在所述气水反应器内达到20米/秒以上的相对运动速度，从而能高效低成本地产生大量负氧离子并净化空气而不产生诸如臭氧的任何有害物质。
较佳的是，所述气水反应器还包括溅板，所述溅板设置在所述气水反应器内以用于使水流在被空气流冲击、摩擦之前被分散。
根据上述技术方案，本发明的用于净化空气的装置能起到以下有益技术效 果：使水流在被高速气流冲击、摩擦之前充分散开，从而能更高效地产生大量负氧离子并净化空气。
附图说明
图1是根据本发明的用于产生负氧离子或用于净化空气的方法和装置的示意图。
图2(a)是本发明第一实施例的用于产生负氧离子或用于净化空气的方法和装置的示意图。图2(b)是沿图2(a)中线A-A所剖取的剖视图。
图3是本发明第二实施例的用于产生负氧离子或用于净化空气的方法和装置的示意图。
图4是本发明第三实施例的用于产生负氧离子或用于净化空气的方法和装置的示意图。
图5(a)是本发明第四实施例的用于产生负氧离子或用于净化空气的方法和装置的示意俯视图。图5(b)是本发明第四实施例的用于产生负氧离子或用于净化空气的方法和装置的示意侧视图。
附图标记列表：
101、气水反应器；
102、气水分离器；
103、引风机；
104、桨轴；
105、桨叶；
106、电动机；
201、气水反应器；
202、气水分离器；
203、引风机；
204、桨轴；
205、桨叶；
206、电动机；
207、水泵；
208、喷水器；
301、气水反应器；
302、气水分离器；
307、水泵；
308、喷水管；
309、竖板；
401、气水反应器；
402、气水分离器；
403、引风机；
408、喷水管；
410、溅板；
411、进气管；
412、入口。
具体实施方式
下面结合具体实施例和附图对本发明作进一步说明，在以下的描述中阐述了更多的细节以便于充分理解本发明，但是本发明显然能够以多种不同于此描述的其它方式来实施，本领域技术人员可以在不违背本发明内涵的情况下根据实际应用情况作大致推广、演绎，因此不应以此具体实施例的内容限制本发明的保护范围。
图1示出了根据本发明的用于产生负氧离子或用于净化空气的方法和装置的示意图。
如图1所示，用于产生负氧离子或用于净化空气的方法包括：
将空气和水分别引入气水反应器，以使引入的空气和水在气水反应器内达到20米/秒以上的相对运动速度而在气水反应器内发生反应，从而产生负氧离子并使空气被净化；以及
将反应之后含负氧离子的净化空气与反应之后的水分离，并将反应之后含负氧离子的净化空气释放到所需空间。
同样如图1所示，用于产生负氧离子或用于净化空气的装置包括：
气水反应器，气水反应器用于分别引入空气和水，以使引入的空气和水在气水反应器内达到20米/秒以上的相对运动速度而在气水反应器内发生反应，从而产生负氧离子并使空气被净化；以及
设置在气水反应器下游的气水分离器，气水分离器用于将反应之后含负氧离子的净化空气与反应之后的水分离，并将反应之后含负氧离子的净化空气释放到所需空间。
由于引入的空气和水在气水反应器内达到20米/秒以上的相对运动速度，水体被空气高速切割、摩擦，空气中生成了大量自由电子，并与氧气结合形成大量负氧离子。负氧离子和水雾(例如在引风机或鼓风机的作用下)进入气水分离器，水回流至气水反应器底部，含负氧离子的净化空气从气水分离器的出气口释放到所需空间。
空气主要组分是氮气、氧气、二氧化碳，含量分别是78％、21％、0.03％，氮气对电子无亲和力，因此只能形成氧气和二氧化碳的负离子。二氧化碳分子、氧分子与负电荷的结合效率基本相同，但空气中二氧化碳浓度只有氧气的1/700，因此负电荷基本都被氧气俘获，成为负氧离子。
同时，水(水雾以及水蒸气)、负氧离子可以高效清除空气中各种粒径的颗粒物，净化空气。具体来说：气水反应器中的水气剧烈相对运动对空气中的大颗粒物(PM2.5以上)有很强的净化作用，而产生的大量负氧离子对空气中的小颗粒物(PM2.5)有很强的净化作用。
对空气中不同粒径颗粒物的清除过程是：
大颗粒物(PM2.5以上)在气水反应器内被水雾洗涤裹挟分离，颗粒增湿增重后分离。
小颗粒物(PM2.5)可分为三类，其中主要是带正电荷的粒子和电中性的粒子，以及极少部分带负电荷的粒子。
带正电荷粒子主要是有机碳分子，如甲醛、苯类等，负氧离子可以使之电中和、聚集、分离。
电中性的粒子，主要是一些病毒和细菌，负氧离子携带的负电荷可以改变微生物遗传物质，使之凋亡。
带负电荷粒子主要是硫酸根、盐酸根、硝酸根以及氯离子等，具备亲水性，可被水雾清除。
更佳的是，引入的空气和水在气水反应器内达到40米/秒以上的相对运动速度而在气水反应器内发生反应。
较佳的是，在气水反应器内的气水反应时间小于1秒。
较佳的是，气水分离器包括离心式分离器或斜板式惯性分离器。在气水分离器采用离心式分离器的情况下，较佳的是，该离心式分离器的旋蜗角度是可调节的。这样，可实现气水分离(脱水)效率可调。
依据本发明可以制造一系列的用于产生负氧离子或用于净化空气的装置，适用于不同容积的室内或者车内或者其他封闭环境。
本发明能提供一种用于产生负氧离子的方法和装置，其能高效低成本地产生大量负氧离子而不产生诸如臭氧的任何有害物质。
本发明还能提供一种用于净化空气的方法和装置，其能高效低成本地净化空气(不论颗粒物的原始浓度和粒径大小，也不限装置的工作时间)且不产生诸如臭氧、氮氧化物等的任何有害物质，且长效免维护。
较佳的是，本发明还有一定的调节空气湿度以及调节空气温度的功能。
第一实施例
图2(a)是本发明第一实施例的用于产生负氧离子或用于净化空气的方法和装置的示意图。图2(b)是沿图2(a)中线A-A所剖取的剖视图。
本发明第一实施例的用于产生负氧离子或用于净化空气的装置包括：
气水反应器101，气水反应器101用于分别引入空气和水，以使引入的空气和水在气水反应器内达到20米/秒以上的相对运动速度而在气水反应器内发生反应，从而产生负氧离子并使空气被净化；以及
设置在气水反应器101下游的气水分离器102，气水分离器102用于将反应之后含负氧离子的净化空气与反应之后的水分离，并将反应之后含负氧离子的净化空气释放到所需空间。
本发明第一实施例的气水反应器101例如是一个由水平放置的直桶状气水反应器。例如，直桶状气水反应器的直径为20厘米，长度为80厘米。
本发明第一实施例的用于产生负氧离子或用于净化空气的装置还可包括引风机103，引风机103有利地设置在气水分离器102下游，用于更为有效地将反应之后含负氧离子的净化空气释放到所需空间。当然，本领域技术人员在本发明的基础上可以理解，也可设置位于其它位置的鼓风机来替代引风机，同样可以更为有效地将反应之后含负氧离子的净化空气释放到所需空间。
本发明第一实施例的用于产生负氧离子或用于净化空气的装置还可包括桨轴104和一组或多组桨叶105。桨叶可以50至500转/分的转速击打在气水反应器101内的水，形成速度为20米/秒以上的水滴，以使水滴与引入的空气碰撞、摩擦。
本发明第一实施例的用于产生负氧离子或用于净化空气的装置还可较佳地包括进气口、出气口、水位控制器、进水口、水泵、电动机、减速机等。
例如，气水反应器101桶身左侧正上方设有一个5＊10厘米的进气口，气水反应器101桶身右侧正上方设有一个5＊10厘米的出气口。
例如，桨轴104长85厘米，贯穿桶身，以密封轴衬与桶身连接。桨轴104末端与气水反应器101外面的减速机(未示出)相连，通过与减速机连接的电动机106进行驱动。桨轴104上较佳地设有20组四叶桨叶105。桨叶105长6厘米，宽1厘米，为一长方形平面设计，厚度为3毫米。每组桨叶105的间隔为2厘米。桶内底部有一个进水口，与水源相连，通过水位控制器将水深控制为6厘米，桶身右侧上方由气水分离器102与出气口相接。气水分离器102较佳地是多管旋风除雾器。气水分离器102底部设有排水口，将分离出来的水回流到气水反应器101中。
运行时，例如，电动机106驱动桨叶105以每秒120转的速度旋转，高速击打液面，产生大量水滴，可将水滴加速到最大每秒43米的速度，加速后的水滴高速切割、摩擦空气，水失去电子，失去的电子成为空间自由电子，空间自由电子与氧气结合形成大量负氧离子。负氧离子和水雾在引风机103的作用下进入气水分离器102，水分离后回流至气水反应器101底部，含负氧离子的空气从气水分离器102出气口排出。
通过气水反应器101后，水和气体进入气水分离器102。在离心力的作用下，各种颗粒物随水体一起最终被分离，流入水箱沉淀，完成清除。空气仅携 带负氧离子返回室内，负氧离子在室内扩散，对室内的PM2.5继续清除。
较佳的是，气水分离器的内壁是平滑的，无凹凸结构。这样，确保了水滴始终保持20米/秒以上的速度。
较佳的是，桨叶的外表面是粗糙的。这样，确保了桨叶击打水面时可有效地带起水滴。
较佳的是，桨叶的横截面呈大致矩形。这样，进一步确保了桨叶击打水面时可有效地带起水滴，并使水滴具备20米/秒以上的速度。
适用于各种封闭空间的用于产生负氧离子或用于净化空气的装置只要调整设备功率以及尺寸即可达到目的。
第二实施例
图3是本发明第二实施例的用于产生负氧离子或用于净化空气的方法和装置的示意图。
本发明第二实施例的用于产生负氧离子或用于净化空气的装置包括：
气水反应器201，气水反应器201用于分别引入空气和水，以使引入的空气和水在气水反应器内达到20米/秒以上的相对运动速度而在气水反应器内发生反应，从而产生负氧离子并使空气被净化；以及
设置在气水反应器201下游的气水分离器202，气水分离器202用于将反应之后含负氧离子的净化空气与反应之后的水分离，并将反应之后含负氧离子的净化空气释放到所需空间。
本发明第二实施例的气水反应器201例如是一个竖直放置的直桶状气水反应器。例如，直桶状气水反应器的直径为20厘米，高度为80厘米。
本发明第二实施例的用于产生负氧离子或用于净化空气的装置还可包括引风机203，引风机203有利地设置在气水分离器202下游，用于更为有效地将反应之后含负氧离子的净化空气释放到所需空间。当然，本领域技术人员在本发明的基础上可以理解，也可设置位于其它位置的鼓风机来替代引风机，同样可以更为有效地将反应之后含负氧离子的净化空气释放到所需空间。
本发明第二实施例的用于产生负氧离子或用于净化空气的装置还可包括桨轴204和一组或多组桨叶205。桨叶可以50至500转/分的转速击打在气水 反应器201内从喷水器208洒落的水，形成速度为20米/秒以上的水滴，以使水滴与引入的空气碰撞、摩擦。
本发明第二实施例的用于产生负氧离子或用于净化空气的装置还可较佳地包括进气口、出气口、进水口、水泵207、电动机206、减速机等。
例如，气水反应器201顶部侧面设有一个5＊10厘米的出气口，在出气口下方10厘米处布置两个直径为9厘米的喷水器208。桨轴204的高度为40厘米，桨轴上4组桨叶的高度均为2厘米，长度为9.6厘米，4组桨叶以角度交错的方式布置在喷水器208下方5厘米至20厘米的区间。气水反应器201距底部20厘米的器壁上开有5＊10厘米的进气口。气水反应器201下部为开放式的水箱，液面高度为10厘米。
运行时，例如，水泵207将水从气水反应器201底部水箱以每秒0.2升的流量从喷水器208喷淋出来。4组叶片在电动机的驱动下同时以每秒120转的转速运行，将喷淋出来的水体高速击打，可将水滴加速到最大每秒72米的速度，加速后的水滴高速切割、摩擦空气，水失去电子，失去的电子成为空间自由电子，空间自由电子与氧气结合形成大量负氧离子。携带水雾和负氧离子的空气从出气口进入气水分离器202，水被分离，回流到水箱。含负氧离子的空气从气水分离器202出气口排出。
适用于各种封闭空间的用于产生负氧离子或用于净化空气的装置只要调整设备功率以及尺寸即可达到目的。
第三实施例
图4是本发明第三实施例的用于产生负氧离子或用于净化空气的方法和装置的示意图。
本发明第三实施例的用于产生负氧离子或用于净化空气的装置包括：
气水反应器301，气水反应器301用于分别引入空气和水，以使引入的空气和水在气水反应器内达到20米/秒以上的相对运动速度而在气水反应器内发生反应，从而产生负氧离子并使空气被净化；以及
设置在气水反应器301下游的气水分离器302，气水分离器302用于将反应之后含负氧离子的净化空气与反应之后的水分离，并将反应之后含负氧离子 的净化空气释放到所需空间。
本发明第三实施例的气水反应器301例如是一个长立方体形的气水反应器。例如，气水反应器301长30厘米，宽20厘米，高60厘米。
本发明第三实施例的用于产生负氧离子或用于净化空气的装置还可较佳地包括进气口、出气口、喷水管308、水泵307等。
例如，气水反应器301上表面开放，上部设置有一竖板309，将箱体分割成长度分别为10厘米和20厘米的两部分，窄侧为进气口，宽侧为出气口。竖板309与箱体上表面平齐，距离箱体底部20厘米。箱体底部为水箱，水深15厘米，并较佳地设置有水位控制器，与水源相连。在窄侧的气水反应器301外表面上设置有2根截面积为1平方毫米的喷水管308，距离箱体顶部15厘米。喷水管308通过水泵307与箱体底部的水箱相连。水泵307压力为0.4MPa，流量每秒1升。宽侧上部设置有气水分离器302。气水分离器302例如是一组倾斜角为55度的斜板式惯性脱水器。箱体上方的出气口与引风机相连。
运行时，例如，水泵307将水流通过喷水管308以0.4MPa的压强喷出，撞击到竖板309上，水流高速切割、摩擦空气，水失去电子，失去的电子成为空间自由电子，空间自由电子与氧气结合形成大量负氧离子。负氧离子和水雾在引风机的作用下进入右侧的气水分离器302(斜板式惯性脱水器)，水分离后回流至气水反应器301底部，含负氧离子的空气从引风机出风口排出。
适用于各种封闭空间的用于产生负氧离子或用于净化空气的装置只要调整设备功率以及尺寸即可达到目的。
第四实施例
图5(a)是本发明第四实施例的用于产生负氧离子或用于净化空气的方法和装置的示意俯视图，图5(b)是本发明第四实施例的用于产生负氧离子或用于净化空气的方法和装置的示意侧视图。
本发明第四实施例的用于产生负氧离子或用于净化空气的装置包括：
气水反应器401，气水反应器401用于分别引入空气和水，以使引入的空气和水在气水反应器内达到20米/秒以上的相对运动速度而在气水反应器内发生反应，从而产生负氧离子并使空气被净化；以及
设置在气水反应器401下游的气水分离器402，气水分离器402用于将反应之后含负氧离子的净化空气与反应之后的水分离，并将反应之后含负氧离子的净化空气释放到所需空间。
这里介绍一个适用于面积为40m2、空间为120m3的本发明第四实施例的用于产生负氧离子或用于净化空气的方法和装置。按20分钟房间空气全部循环一次，则风机流量是120m3/20min＝360m3/h＝0.1m3/s，风压为2500Pa。
例如，空气被风机从截面积200cm2的进气口吸入进气管411(也可称为“进气部”)，空气速度为5m/s，在进气管的末端，管道截面缩小，使空气速度加快到40m/s(当然，这里的空气速度40m/s只是一种示例，在本发明的原理下，只要采用速度为20米/秒以上的空气流即可)，进入气水反应器401的入口412，在入口412前用水泵和喷水管408向气水反应器401内喷水，水冲向入口412前的溅板410散开后，被高速气流反复切割、摩擦，水失去电子，失去的电子成为空间自由电子，空间自由电子与氧气结合形成大量负氧离子。同时，在气水反应器401形成大量水雾和水蒸气。
负氧离子和水雾例如在引风机403的作用下进入右侧的气水分离器402。在离心力的作用下，各种颗粒物随水体一起最终被分离，流入水箱沉淀，完成清除。空气仅携带负氧离子和部分水蒸气返回室内，负氧离子在室内扩散，对室内的PM2.5继续清除。
较佳的是，引入的水和空气的体积比为5:1000至50:1000。
较佳的是，速度为20米/秒以上的空气流由进气道变径产生。
本方法和装置对流经气水反应器内的空气中各粒径颗粒物的一次清除率可达到95％以上。
适用于各种封闭空间的用于产生负氧离子或用于净化空气的装置只要调整设备功率以及尺寸即可达到目的。
虽然上述给出的四个实施例描述了特定构造的用于产生负氧离子或用于净化空气的方法和装置，但本领域技术人员在本发明的基础上可以理解，本发明的保护范围并不局限于以上列举的特定构造的用于产生负氧离子或用于净化空气的方法和装置，而也可采用其它构造的用于产生负氧离子或用于净化空 气的方法和装置。根据本发明的原理，只要用于产生负氧离子或用于净化空气的方法包括如下步骤即可：将空气和水分别引入气水反应器，以使引入的空气和水在气水反应器内达到20米/秒以上的相对运动速度而在气水反应器内发生反应，从而产生负氧离子并使空气被净化；以及将反应之后含负氧离子的净化空气与反应之后的水分离，并将反应之后含负氧离子的净化空气释放到所需空间。或者，根据本发明的原理，只要用于产生负氧离子或用于净化空气的装置包括如下的气水反应器和气水分离器即可：气水反应器用于分别引入空气和水，以使引入的空气和水在气水反应器内达到20米/秒以上的相对运动速度而在气水反应器内发生反应，从而产生负氧离子并使空气被净化；气水分离器设置在气水反应器下游，气水分离器用于将反应之后含负氧离子的净化空气与反应之后的水分离，并将反应之后含负氧离子的净化空气释放到所需空间。
除了产生负氧离子和净化空气的功能之外，较佳的是，本发明还可具有调温调湿的功能，即，本发明可以是一种以新原理运作的空气调节装置。
较佳的是，用于产生负氧离子或用于净化空气的方法还包括：在将水引入气水反应器之前，调节水的温度，从而调节所释放的空气的温度。
较佳的是，用于产生负氧离子或用于净化空气的装置还包括水温调节器，水温调节器用于在将水引入气水反应器之前，调节水的温度，从而调节所释放的空气的温度。
本发明调节空气温度的原理如下：只要调节引入气水反应器的水的温度，即可调节所释放空气的温度，因为在气水反应器中，水体与空气充分混合，两者直接交换热量，从而快速改变所释放空气的温度。
本发明还可调节空气湿度，其原理如下：在干燥季节，因为本发明的输出气流含有水汽，因此可以给室内加湿；在高湿季节，本发明的气水反应器将室内高湿空气吸入后，将其中一部分的水汽凝结液化并在脱水器中与空气分离，不再进入室内，降低室内湿度。
较佳的是，本发明可以作为一种新原理空调使用，其意义有三：
一、传统空调都是间接加热或者冷却空气，而本发明是使水和空气直接接触进行热交换，效率大大提高。
二、传统空调输出的空气都是干燥空气，人体会感觉不适，而本发明可以 将室内维持一个宜居的相对湿度环境。
三、传统空调无法去除空气中PM2.5以及有害气体如甲醛，也无法产生负氧离子以改善空气质量，本发明可以同时实现上述功能。
上面结合附图对本发明进行了示例性描述，显然本发明的具体实现并不受上述实施方式的限制。本领域技术人员可在不偏离本发明技术构思的前提下，对本发明作出各种修改或变型，这些修改或变型当然也落入本发明的保护范围之内。

Claims (24)

  1. 一种用于产生负氧离子的方法，其特征在于，所述用于产生负氧离子的方法包括：
    将空气和水分别引入气水反应器，以使引入的空气和水在所述气水反应器内达到20米/秒以上的相对运动速度而在所述气水反应器内发生反应，从而产生负氧离子；以及
    将反应之后含负氧离子的空气与反应之后的水分离，并将反应之后含负氧离子的空气释放到所需空间。
  2. 如权利要求1所述的用于产生负氧离子的方法，其特征在于，引入的水和空气的体积比为5:1000至50:1000。
  3. 如权利要求1所述的用于产生负氧离子的方法，其特征在于，引入的空气和水在所述气水反应器内达到20米/秒以上的相对运动速度通过以下方式来实现：由转速为50至500转/分的桨叶击打在所述气水反应器内的水，形成速度为20米/秒以上的水滴，以使水滴与引入的空气碰撞、摩擦。
  4. 如权利要求1所述的用于产生负氧离子的方法，其特征在于，引入的空气和水在所述气水反应器内达到20米/秒以上的相对运动速度通过以下方式来实现：由速度为20米/秒以上的空气流冲击、摩擦水流。
  5. 如权利要求4所述的用于产生负氧离子的方法，其特征在于，在由速度为20米/秒以上的空气流冲击、摩擦水流之前，使水流被设置在所述气水反应器内的溅板分散。
  6. 如权利要求1所述的用于产生负氧离子的方法，其特征在于，所述用于产生负氧离子的方法还包括：在将水引入所述气水反应器之前，调节水的温度，从而调节所释放的空气的温度。
  7. 一种用于产生负氧离子的装置，其特征在于，所述用于产生负氧离子的装置包括：
    气水反应器，所述气水反应器用于分别引入空气和水，以使引入的空气和水在所述气水反应器内达到20米/秒以上的相对运动速度而在所述气水反应器内发生反应，从而产生负氧离子；以及
    设置在所述气水反应器下游的气水分离器，所述气水分离器用于将反应之后含负氧离子的空气与反应之后的水分离，并将反应之后含负氧离子的空气释放到所需空间。
  8. 如权利要求7所述的用于产生负氧离子的装置，其特征在于，引入的水和空气的体积比为5:1000至50:1000。
  9. 如权利要求7所述的用于产生负氧离子的装置，其特征在于，所述气水反应器包括桨叶，所述桨叶用于以50至500转/分的转速击打在所述气水反应器内的水，形成速度为20米/秒以上的水滴，以使水滴与引入的空气碰撞、摩擦。
  10. 如权利要求7所述的用于产生负氧离子的装置，其特征在于，所述气水反应器包括进气部，所述进气部用于使空气流达到20米/秒以上的速度，以冲击、摩擦水流。
  11. 如权利要求10所述的用于产生负氧离子的装置，其特征在于，所述气水反应器还包括溅板，所述溅板设置在所述气水反应器内以用于使水流在被空气流冲击、摩擦之前被分散。
  12. 如权利要求7所述的用于产生负氧离子的装置，其特征在于，所述用于产生负氧离子的装置还包括水温调节器，所述水温调节器用于在将水引入所述气水反应器之前，调节水的温度，从而调节所释放的空气的温度。
  13. 一种用于净化空气的方法，其特征在于，所述用于净化空气的方法包括：
    将空气和水分别引入气水反应器，以使引入的空气和水在所述气水反应器内达到20米/秒以上的相对运动速度而在所述气水反应器内发生反应，从而产生负氧离子并使空气被净化；以及
    将反应之后含负氧离子的净化空气与反应之后的水分离，并将反应之后含负氧离子的净化空气释放到所需空间。
  14. 如权利要求13所述的用于净化空气的方法，其特征在于，引入的水和空气的体积比为5:1000至50:1000。
  15. 如权利要求13所述的用于净化空气的方法，其特征在于，引入的空气和水在所述气水反应器内达到20米/秒以上的相对运动速度通过以下方式来实 现：由转速为50至500转/分的桨叶击打在所述气水反应器内的水，形成速度为20米/秒以上的水滴，以使水滴与引入的空气碰撞、摩擦。
  16. 如权利要求13所述的用于净化空气的方法，其特征在于，引入的空气和水在所述气水反应器内达到20米/秒以上的相对运动速度通过以下方式来实现：由速度为20米/秒以上的空气流冲击、摩擦水流。
  17. 如权利要求16所述的用于净化空气的方法，其特征在于，在由速度为20米/秒以上的空气流冲击、摩擦水流之前，使水流被设置在所述气水反应器内的溅板分散。
  18. 如权利要求13所述的用于净化空气的方法，其特征在于，所述用于净化空气的方法还包括：在将水引入所述气水反应器之前，调节水的温度，从而调节所释放的净化空气的温度。
  19. 一种用于净化空气的装置，其特征在于，所述用于净化空气的装置包括：
    气水反应器，所述气水反应器用于分别引入空气和水，以使引入的空气和水在所述气水反应器内达到20米/秒以上的相对运动速度而在所述气水反应器内发生反应，从而产生负氧离子并使空气被净化；以及
    设置在所述气水反应器下游的气水分离器，所述气水分离器用于将反应之后含负氧离子的净化空气与反应之后的水分离，并将反应之后含负氧离子的净化空气释放到所需空间。
  20. 如权利要求19所述的用于净化空气的装置，其特征在于，引入的水和空气的体积比为5:1000至50:1000。
  21. 如权利要求19所述的用于净化空气的装置，其特征在于，所述气水反应器包括桨叶，所述桨叶用于以50至500转/分的转速击打在所述气水反应器内的水，形成速度为20米/秒以上的水滴，以使水滴与引入的空气碰撞、摩擦。
  22. 如权利要求19所述的用于净化空气的装置，其特征在于，所述气水反应器包括进气部，所述进气部用于使空气流达到20米/秒以上的速度，以冲击、摩擦水流。
  23. 如权利要求22所述的用于净化空气的装置，其特征在于，所述气水反应器还包括溅板，所述溅板设置在所述气水反应器内以用于使水流在被空气流 冲击、摩擦之前被分散。
  24. 如权利要求23所述的用于净化空气的装置，其特征在于，所述用于净化空气的装置还包括水温调节器，所述水温调节器用于在将水引入所述气水反应器之前，调节水的温度，从而调节所释放的净化空气的温度。
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113834126A (zh) * 2021-10-14 2021-12-24 深圳市百宏怡氧技术有限公司 一种气激式负氧离子空调机

Families Citing this family (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103893810B (zh) 2014-04-17 2017-01-04 刘晓岳 用于产生负氧离子的方法和装置及用于净化空气的方法和装置
CN108592231A (zh) * 2017-06-15 2018-09-28 任庆田 空气负离子补充机
CN108211622B (zh) * 2018-01-19 2023-07-14 苏州银雀智能科技有限公司 一种快速除霾r型工程车
CN110160173A (zh) * 2018-02-12 2019-08-23 广东天物新材料科技有限公司 一种负离子蒸汽和用途及其制备方法
CN111790233A (zh) * 2019-04-08 2020-10-20 廊坊鹏帮木业有限公司 一种可净化空气的负离子液及其制备方法和应用
CN112762565A (zh) * 2019-11-06 2021-05-07 重庆艾犇健康科技有限公司 一种被动式康养系统
CN113606720B (zh) * 2021-07-03 2023-09-12 李晓东 瀑布式负氧离子发生器
CN113685952B (zh) * 2021-07-08 2023-03-24 深圳市宏康环境科技有限公司 大空间负氧离子设备
CN113813701A (zh) * 2021-10-19 2021-12-21 深圳市宏康环境科技有限公司 一种除冷凝水装置及负氧离子发生设备
CN114632247A (zh) * 2022-03-29 2022-06-17 深圳微子医疗有限公司 一种供氢氧装置

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0554591A1 (en) * 1992-02-04 1993-08-11 Scat Equipment Pte Ltd. Ionizer
CN2257363Y (zh) * 1996-01-10 1997-07-02 张斌香 室内空气清新器
JPH09203540A (ja) * 1996-01-29 1997-08-05 Fine:Kk 陰イオン発生方法及び装置
CN103893810A (zh) * 2014-04-17 2014-07-02 刘晓岳 用于产生负氧离子的方法和装置及用于净化空气的方法和装置
CN203943933U (zh) * 2014-04-17 2014-11-19 刘晓岳 用于产生负氧离子的装置及用于净化空气的装置

Family Cites Families (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5728288A (en) * 1995-08-30 1998-03-17 Yugenkaisha Kubo Technical Office Apparatus and method for producing air containing minus alkali ion
JPH10300139A (ja) * 1997-05-01 1998-11-13 Tiger Vacuum Bottle Co Ltd 負イオン発生装置
EP1175229B1 (en) * 1999-05-06 2004-12-29 Intecon Systems, Inc. Cleaning particulate matter and chemical contaminants from hands
AU2003223649A1 (en) * 2002-04-16 2003-11-03 Prompt Care, Inc. Method for abatement of allergens, pathogens and volatile organic compounds
WO2004062800A1 (en) * 2003-01-06 2004-07-29 The Johns Hopkins University Hydroxyl free radical-induced decontamination of airborne spores, viruses and bacteria in a dynamic system
US7695692B2 (en) * 2003-08-06 2010-04-13 Sanderson William D Apparatus and method for producing chlorine dioxide
WO2007026363A2 (en) * 2005-09-01 2007-03-08 Megair Ltd. Method and apparatus for treating biologically contaminated air
KR100604425B1 (ko) * 2006-01-23 2006-07-25 운해이엔씨(주) 비방전식 산업용 공기정화 장치
RU2348871C1 (ru) * 2007-08-22 2009-03-10 Вадим Иванович Алферов Устройство для сжижения и сепарации газов
JP2012249988A (ja) * 2011-06-07 2012-12-20 Panasonic Corp 電気掃除機
CN203183866U (zh) * 2013-02-02 2013-09-11 郑州大学 筛网除尘负氧离子换气机
CN203264047U (zh) * 2013-03-26 2013-11-06 王刚 强磁旋流自发电负氧离子发生器

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0554591A1 (en) * 1992-02-04 1993-08-11 Scat Equipment Pte Ltd. Ionizer
CN2257363Y (zh) * 1996-01-10 1997-07-02 张斌香 室内空气清新器
JPH09203540A (ja) * 1996-01-29 1997-08-05 Fine:Kk 陰イオン発生方法及び装置
CN103893810A (zh) * 2014-04-17 2014-07-02 刘晓岳 用于产生负氧离子的方法和装置及用于净化空气的方法和装置
CN203943933U (zh) * 2014-04-17 2014-11-19 刘晓岳 用于产生负氧离子的装置及用于净化空气的装置

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See also references of EP3132807A4 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113834126A (zh) * 2021-10-14 2021-12-24 深圳市百宏怡氧技术有限公司 一种气激式负氧离子空调机

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