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WO2017012538A1 - 大气甘露转化系统 - Google Patents

大气甘露转化系统 Download PDF

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Publication number
WO2017012538A1
WO2017012538A1 PCT/CN2016/090612 CN2016090612W WO2017012538A1 WO 2017012538 A1 WO2017012538 A1 WO 2017012538A1 CN 2016090612 W CN2016090612 W CN 2016090612W WO 2017012538 A1 WO2017012538 A1 WO 2017012538A1
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Prior art keywords
water
air
drinking
tank
casing
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Ceased
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PCT/CN2016/090612
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English (en)
French (fr)
Inventor
吴达镕
吴慈欣
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Individual
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Individual
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Priority to JP2018522840A priority Critical patent/JP2018528860A/ja
Publication of WO2017012538A1 publication Critical patent/WO2017012538A1/zh
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
    • B01D5/0078—Condensation of vapours; Recovering volatile solvents by condensation characterised by auxiliary systems or arrangements
    • B01D5/009—Collecting, removing and/or treatment of the condensate
    • 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
    • A61L9/01—Deodorant compositions
    • A61L9/014—Deodorant compositions containing sorbent material, e.g. activated carbon
    • 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
    • A61L9/18—Radiation
    • A61L9/20—Ultraviolet radiation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
    • B01D5/0057—Condensation of vapours; Recovering volatile solvents by condensation in combination with other processes
    • B01D5/0072—Condensation of vapours; Recovering volatile solvents by condensation in combination with other processes with filtration
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00—Multistage treatment of water, waste water or sewage
    • C02F9/20—Portable or detachable small-scale multistage treatment devices, e.g. point of use or laboratory water purification systems
    • E—FIXED CONSTRUCTIONS
    • E03—WATER SUPPLY; SEWERAGE
    • E03B—INSTALLATIONS OR METHODS FOR OBTAINING, COLLECTING, OR DISTRIBUTING WATER
    • E03B3/00—Methods or installations for obtaining or collecting drinking water or tap water
    • E03B3/28—Methods or installations for obtaining or collecting drinking water or tap water from humid air
    • 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
    • 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
    • A61L2209/00—Aspects relating to disinfection, sterilisation or deodorisation of air
    • A61L2209/10—Apparatus features
    • A61L2209/11—Apparatus for controlling air treatment
    • A61L2209/111—Sensor means, e.g. motion, brightness, scent, contaminant sensors
    • 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
    • A61L2209/00—Aspects relating to disinfection, sterilisation or deodorisation of air
    • A61L2209/10—Apparatus features
    • A61L2209/14—Filtering means
    • 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
    • C02F1/008—Control or steering systems not provided for elsewhere in subclass C02F
    • 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
    • C02F1/02—Treatment of water, waste water, or sewage by heating
    • C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
    • C02F1/048—Purification of waste water by evaporation
    • 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
    • C02F1/02—Treatment of water, waste water, or sewage by heating
    • C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
    • C02F1/18—Transportable devices to obtain potable water
    • 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
    • C02F1/28—Treatment of water, waste water, or sewage by sorption
    • C02F1/283—Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
    • 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
    • C02F1/30—Treatment of water, waste water, or sewage by irradiation
    • C02F1/32—Treatment of water, waste water, or sewage by irradiation with ultraviolet light
    • C02F1/325—Irradiation devices or lamp constructions
    • 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
    • C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
    • C02F1/441—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
    • 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
    • C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/46104—Devices therefor; Their operating or servicing
    • 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
    • C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/46104—Devices therefor; Their operating or servicing
    • C02F1/4618—Devices therefor; Their operating or servicing for producing "ionised" acidic or basic water
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00—Controlling or monitoring parameters in water treatment
    • C02F2209/02—Temperature
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00—Controlling or monitoring parameters in water treatment
    • C02F2209/42—Liquid level
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00—Specific treatment goals
    • C02F2303/04—Disinfection
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00—Specific treatment goals
    • C02F2303/24—Separation of coarse particles, e.g. by using sieves or screens
    • Y—GENERAL 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
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00—Water conservation; Efficient water supply; Efficient water use
    • Y—GENERAL 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
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00—Water conservation; Efficient water supply; Efficient water use
    • Y02A20/152—Water filtration

Definitions

  • the present invention relates to an atmospheric mannose conversion system device, and more particularly to an air purification device and a water production device
  • it relates to a part of an air purifying device capable of releasing negative oxygen ions and a system for extracting high-quality, clean, sterile, non-toxic, acid-base neutral water in three-in-one water from the moisture in the air. Water equipment part.
  • Freshwater resources are not only in short supply, but also heavily polluted and extremely unevenly distributed, even where electricity and energy are abundant. Clean water resources may still be lacking, so water resources are becoming a valuable resource, and water resources issues have become a major strategy related to national economic and social sustainable development and long-term stability.
  • Atmospheric mannose conversion system equipment can be used in small household and industrial large-volume water source and air conversion systems, on the one hand to remove excess water and atmospheric pollutants in the air, to purify the air, to control indoor air humidity; The excess water is converted into potable health water, and the tap water or other non-potable water is converted into potable health water, so that the indoor air and drinking water are improved at the same time.
  • an atmospheric mannose conversion system apparatus comprising an air purification equipment portion capable of releasing negative oxygen ions and extracting high quality, clean, sterile, non-toxic, acid from moisture in the air.
  • Alkaline neutral water three-in-one water-making equipment part of drinking water.
  • the air purifying device adjusts whether the dehumidification function is activated according to the humidity of the air to prepare fresh air rich in negative oxygen ions; the water making device adjusts the amount of water according to the amount of water in the air, and in some high humidity marine and inland climate regions, it The amount of water produced is large. In some areas where the pollution or water quality is not drinkable, it can be purified into direct drinking water through primary filtration and secondary filtration, sterilization and disinfection systems.
  • the purified water can be used from domestic water to drinking water for industrial and commercial use.
  • An atmospheric mannose conversion system apparatus comprising an air purification equipment section 1 and a water production equipment section 2.
  • the air purification device portion 1 includes a housing 11 and a filter unit disposed in the housing, and the filter unit includes a filter screen 12, a fiber cloth layer 13, an activated carbon mesh layer 14, a drive motor 15, and an orifice plate 16,
  • the top end of the filter net 12 is provided with a fiber cloth layer 13 , and an activated carbon net 14 is disposed above the fiber cloth layer 13 .
  • the filter net 12 , the fiber cloth layer 13 , and the activated carbon net layer 14 are arranged in parallel with each other.
  • the orifice plate 16 is disposed above the activated carbon mesh layer 14.
  • the orifice plate 16 is fixedly connected to the inner wall of the casing 1.
  • the orifice plate 16 is fixedly mounted for driving.
  • a driving motor 15 of the impeller 17, an output shaft of the driving motor 15 is connected to the impeller 17, and a top end of the casing 11 is provided with an exhausting plate 18 between the exhausting plate 18 and the orifice plate 16
  • An ultraviolet germicidal lamp 19 is provided, and a control panel 110 is disposed on the outer side wall of the step of the casing 11.
  • the water making device part 2 includes a casing 21 on which a control panel 225, a humidity controller 22, an air passage net 23, a condensing evaporator 24, a water collecting tray 25, a water collecting tank 26, a water collecting tank are disposed.
  • the air purifying device portion 1 and the water making device portion 2 are connected by a pipe 00 which is connected between the exhausting plate 18 and the air passing through the mesh 23.
  • the working principle of the atmospheric mannose conversion system device is that the impeller 17 is controlled to rotate by the driving motor 15, and the air enters the inside of the casing 11 from the shell hole, and then the filter net 12, the fiber cloth layer 13, and the activated carbon net 14 are sequentially paired with air. After the treatment, the treated air passes through the orifice plate 16 and then sterilizes the air through the ultraviolet germicidal lamp 19. The purified air is discharged from the pipeline 00 to the air passing through the mesh 23 by the exhaust panel 18, and is controlled by the humidity control regulator. 22.
  • the air extraction water system consisting of the exhaust fan 17, the condensing evaporator 24, and the compressor 220, the air is cooled by the condensing evaporator 24 to a temperature of the dew point; at the temperature of the dew point, the moisture of the air is extracted and condensed into water.
  • the beads and the water droplets are automatically dropped from the condensing evaporator onto the water collecting tray 25, and the water collecting tray 25 collects the water into the water collecting tank 26, and the water collecting tank 26 controls the boosting pump 28 connected to the water collecting tank according to the water level controller 27 to increase the water.
  • the built-in water level display and the bottom of the clean water tank are respectively connected with the drinking neutral water valve 16 and the electrolytic tank 213 for the user to choose to discharge the neutral water or pass through the electrolytic tank 213, and the acid water is released from the drinking acid water valve 214 and the drinking alkali water valve 215. Or alkaline water.
  • the purified and dehumidified air after the air extraction water system consisting of the humidity control regulator 22, the exhaust fan 17, the condensing evaporator 24, and the compressor 220 of the water making device portion 2 passes through the condensing evaporator 24 through the negative oxygen ion generator After 226, it is discharged through the exhaust plate 223
  • the humidity of the preliminary treatment air discharged from the air exhaust plate 18 of the air cleaning device portion 1 by the humidity controller controller 22 is sufficient to raise the moisture in the air, and if the air humidity is too low, less than 38% Then, the air extraction water system consisting of the exhaust fan 17, the condensing evaporator 24, and the compressor 220 stops functioning, and only uses the function of adjusting the air temperature; and the water source 227 is passed by tap water or the drinking standard.
  • the pump 28 is added to the atmospheric mannose conversion system apparatus, and the filtration system 29, the reverse osmosis purification system 210, and the nano-ultraviolet sterilizer 211 are connected.
  • the air purifying device portion 1 of the atmospheric mannose conversion system device is connected to the outside to process the air drawn in from the outside, and is discharged to the indoor through the water-making device portion 2 After purifying and adding high quality air of negative oxygen ions.
  • Tap water or water source 227 that does not meet the drinking standard can be treated by an external primary filter. For example, if the water source is poor, the particle carbon filter and the activated carbon filter need to be added, the dye in the water is filtered, and then the atmospheric mannose is converted. The booster pump 28 of the system water machine.
  • the atmospheric mannose conversion system device can filter dust, smoke, dust, cotton linters, animal dander, mites, pollen, mold spores and bacteria particles in the air through the air purification device portion 1 through the water making device part 2 Control air humidity and increase negative oxygen ions, discharge clean air into the room, and the same function can adjust the air temperature; and the water production equipment part 2 can produce high quality, clean, sterile, non-toxic, acid-base neutral Water three-in-one drinking water, the atmospheric mannose conversion system equipment integrates the functions of air conditioner, air purifier, pure water machine and acid-base water machine, which is a more advantageous equipment.
  • FIG. 1 is a schematic diagram of an apparatus for atmospheric mannose conversion system.
  • 1 is an air purifying device portion; 2 is a water producing device portion; the air purifying device portion 1 is connected to the water making device portion 2 through a pipe 00.
  • FIG. 2 is a partial schematic view of an air cleaning device.
  • FIG. 3-1 is a front view of a portion of a water making device
  • FIG. 3-2 is a schematic diagram showing the internal structure of a water-making device
  • FIG. 3-3 Schematic diagram of the back part of the water making device
  • FIG. 4 is a schematic diagram of the operation of the condensing evaporator 24.
  • FIG. 5 is a flow chart and schematic diagram of a reverse osmosis purification system 210
  • the principle of the main working principle of the reverse osmosis membrane system is that it uses reverse osmosis membrane technology. Its working principle is to exert a certain pressure on the water, so that the water molecules and the ionic mineral elements pass through the reverse osmosis membrane and dissolve in the water.
  • the vast majority of inorganic salts (including heavy metals), organic matter, bacteria, viruses, etc., are impervious to the reverse osmosis membrane, so that the permeated pure water and the impervious concentrated water are strictly separated;
  • the pore size on the reverse osmosis membrane is only 0.0001 ⁇ m, while the diameter of the virus is generally 0.02-0.4 ⁇ m, and the diameter of the common bacteria is 0.4-1 ⁇ m, so you can safely drink the clear spring flowing out of the pure water machine.
  • FIG. 6 is a working principle diagram of the nano ultraviolet sterilization sterilizer 211
  • the nano UV sterilizer cylinder is made of stainless steel, and the inner wall is polished to improve the ultraviolet ray reflection ability and the radiant intensity, and the amount of the ultraviolet lamp can be adjusted according to the amount of the treated water.
  • Some sterilizers are equipped with spiral vanes on the inner wall of the cylinder to change the movement of the water flow to avoid stagnant water and pipeline blockage. The turbulence generated and the sharp edges of the blades will break the suspended solids and completely expose the attached microorganisms. In the ultraviolet radiation, the disinfection efficiency is improved.
  • the disinfection principle of the nano-ultraviolet sterilizer mainly from ultraviolet ray sterilization using ultraviolet light of 254 nm wavelength.
  • This wavelength of ultraviolet light can destroy the DNA of a cell's life core, thus preventing cell regeneration and loss of regenerative capacity, making the bacteria harmless and achieving sterilization.
  • the size of such a system depends on the intensity of the UV (the intensity and power of the illuminator) and the length of the contact between the water (liquid, liquid, or air exposed to UV light).
  • FIG. 7 is a schematic diagram of the working principle of the negative oxygen ion generator 26.
  • the negative ion generator 26 is composed of a casing 30, and a foamed nickel mesh first electrode 34, a gauze insulating layer 35, a stainless steel mesh second electrode 36, and a voltage conversion circuit 32 fixedly mounted on the inner surface of the casing to cover the nano titanium dioxide.
  • the first electrode 34, the gauze insulating layer 35 and the second electrode 36 are closely attached to each other to constitute a component 37 having a capacitive characteristic.
  • the assembly 37 is in intimate contact with the housing 30 at a mounting and mounting contact surface to prevent air leakage.
  • the housing 30 is provided with an air inlet 31 and an air outlet 33.
  • the oxygen negative ion generator is powered by a 12V battery (not shown).
  • the working principle of the negative oxygen ion generator is: air enters the interior of the negative oxygen ion generator from the air inlet 31, wherein the oxygen contacts the first electrode 34, and a redox reaction occurs, generating an oxygen negative ion, and the oxygen negative ion accompanying the air flow. It flows out from the air outlet 33.
  • FIG. 8 is a flow chart of the operation of the atmospheric mannose conversion system equipment.
  • the impeller 17 is controlled to rotate by the driving motor 15, and the air enters the inside of the casing 11 from the casing hole, and the filter net 12, the fiber cloth layer 13, and the activated carbon net 14 sequentially process the air, and the treated air passes through the orifice plate. 16
  • the air is sterilized by the ultraviolet germicidal lamp 19, and the purified air is discharged from the duct 00 to the air passing through the net 23 by the exhaust panel 18.
  • the humidity control regulator 22 detects that the air entering from the air passing through the net 23 has a humidity of more than 55% and a humidity of 65%, and is composed of a humidity control regulator 22, an exhaust fan 17, a condensing evaporator 24, and a compressor 220.
  • the air extraction water system starts to work, and the air is cooled by the condensing evaporator 24 to the temperature of the dew point; at the dew point temperature, the water is extracted and condensed into water droplets, and the water droplets are automatically dropped from the condensing evaporator.
  • the water collecting tray 25 collects the water into the water collecting tank 26, and the water collecting tank 26 controls the boosting pump 28 connected to the water collecting tank according to the water level controller 27 to pressurize the water, and the water is sent to the filtering system 29 to be generally small.
  • the impurities are removed; and the reverse osmosis purification system 210 separates most of the inorganic salts (including heavy metals), organic substances, bacteria and viruses dissolved in water by adsorption, ultrafiltration and ultra-purification, and directly converts the water quality into ultrapure water;
  • the ultrapure water is connected to the nano-ultraviolet sterilizer 211, and then purified and stored in the water purification tank.
  • the water level display and the bottom of the water tank are respectively connected to the drinking neutral.
  • Valve 16 and the electrolytic cell 213 for the user to select or neutral water discharged through the electrolytic cell 213, 214 by the drinking valve acid, alkaline drinking discharge valve 215 Acid or base.
  • the purified and dehumidified air after the air extraction moisture system composed of the humidity control regulator 22, the exhaust fan 17, the condensing evaporator 24, and the compressor 220 of the water making device portion 2 passes through the negative oxygen ion generator 226 and is exhausted.
  • the plate 223 is discharged.
  • the impeller 17 is controlled to rotate by the driving motor 15, and the air enters the inside of the casing 11 from the casing hole, and then the filter net 12, the fiber cloth layer 13, and the activated carbon net 14 sequentially process the air, and the treated air passes through the orifice plate. 16
  • the air is sterilized by the ultraviolet germicidal lamp 19, and the purified air is discharged from the duct 00 to the air passing through the net 23 by the exhaust panel 18.
  • the humidity control regulator 22 detects that the air entering from the air passing through the net 23 has a humidity of less than 38%, and the humidity is 35%, the air extraction water system consisting of the humidity control regulator 22, the exhaust fan 17, the condensing evaporator 24, and the compressor 220 stops the pumping operation, and changes to the temperature of the conditioned air, and the air is cooled by the condensing evaporator 24. To the right temperature.
  • the booster pump 28 in the atmospheric mannose conversion system device is connected to the filter system 29, the reverse osmosis purification system 210 and the nano-ultraviolet sterilizer 211 by tap water or a drinking water source 227 that does not reach the drinking standard, and is again purified and stored in the water purification tank.
  • the water tank display and the bottom of the water tank are respectively connected with the drinking neutral water valve 16 and the electrolytic tank 213 for the user to choose to discharge the neutral water or pass through the electrolytic tank 213, and the acid water valve 214 and the drinking alkali water valve 215 release the acid water or Alkaline water.
  • the purified and dehumidified air after the air extraction water system composed of the humidity control regulator 22, the exhaust fan 17, the condensing evaporator 24, and the compressor 220 of the water making device portion 2 passes through the negative oxygen ion generator 226
  • the wind plate 223 is discharged.

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Public Health (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Water Supply & Treatment (AREA)
  • Environmental & Geological Engineering (AREA)
  • Veterinary Medicine (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Hydrology & Water Resources (AREA)
  • Epidemiology (AREA)
  • Animal Behavior & Ethology (AREA)
  • General Health & Medical Sciences (AREA)
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  • Organic Chemistry (AREA)
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Abstract

一种大气甘露转化系统设备，包括空气净化设备部分(1)和制水设备部分(2)；空气净化设备部分(1)包括过滤单元；过滤单元包括过滤网(12)、纤维布层(13)、活性炭网层(14)、驱动电机(15)、孔板(16)、叶轮(17)、排风口(18)、紫外杀菌灯(19)和控制面板(110)；制水设备部分包括控制面版(225)、湿度控制器(22)、空气通过网(23)、冷凝蒸发器(24)、集水盘(25)、集水箱(26)、集水箱水位控制器(27)、增压泵(28)、过滤系统(29)、反渗透净化系统(210)、纳米紫外线杀菌消毒器(211)、恒温净水缸(212)、电解槽(213)、饮用酸水阀(214)、饮用碱水阀(215)、饮用中性水阀(216)、抽风机(217)、压缩机(220)、排风板(223)、负氧离子发生器(226)、自来水或不能饮用水源入口(227)。

Description

说明书 发明名称：大气甘露转化系统 技术领域
[0001] 本发明涉及一种大气甘露转化系统设备， 具体的涉及空气净化设备和制水设备
， 更为具体的涉及一种能释放负氧离子的空气净化设备部分和从空气中的水份 提取出优质、 清洁、 无菌、 无毒害、 酸碱中性水三合一的饮用水的制水设备机 部分。
背景技术
[0002] 目前人类比较容易利用淡水资源， 主要来自河流、 湖泊及浅层地下水， 淡水资 源在大量使用下不仅短缺， 加上污染严重而且地区分布极不平衡， 即使电和能 源都充沛的地方， 清洁的水资源仍然可能很缺乏， 所以水资源正在变成一种宝 贵的资源， 水资源问题， 更成为关系到国家经济、 社会可持续发展和长治久安 的重大战略。
[0003] 在一些难获得清洁及缺乏水源的偏远地方， 是很难地铺设一条长距离供水的长 输管线提供饮用水， 或不计算运输成本通过运输工具， 往返运送饮用水， 这些 的方法会把使水的成本变得非常高， 非人般老百姓能接受及享用生活必须的饮 用水， 除了成本非常高外， 也可能因长距离的输送或运送， 导致水质的变化或 污染， 最后人们也无法直接饮用。
[0004] 另外人们在饮用水的需求量不一定很大 (按照不同地区、 不同的气候及不同的 环境需求量不同）， 但其卫生、 清洁、 无菌、 无毒害的要求则较高， 基本上要求 是一致， 我们如何在有能源及电力的地方， 在合理的成本下制做清纯饮水 (人们 以此为甘露）， 所以利用大气 (空气)提取及生产饮用水， 成为国家发展的迫切及 急需要解决的问题。
[0005] 大气甘露转化系统设备可以家居小用量及工业大用量的水源及空气转化系统， 一方面去除空气中过量水和大气污染成分， 净化空气， 控制室内空气湿度； 另 一方面从把空气中的过量水转化为可饮用的保健水， 以及把自来水或者其他非 饮用水转化为可饮用的保健水， 使得室内的空气和饮用水同吋得到改善， 适合 一些对水质及空气质量要求高的家庭 (儿童及老年人等)。
技术问题
问题的解决方案
技术解决方案
[0006] 本发明的目的在于提供一种大气甘露转化系统设备， 该系统包括能释放负氧离 子的空气净化设备部分和从空气中的水份提取出优质、 清洁、 无菌、 无毒害、 酸碱中性水三合一的饮用水的制水设备机部分。 空气净化设备根据空气的湿度 调节是否启动除湿功能， 制备富含负氧离子的新鲜空气； 制水设备机根据空气 的水份多少来调节水量， 在一些湿度高的海洋及内陆气候地区， 它的制水量大 。 在一些受污染或水质不能饮用的地区可以通过初级过滤及二级的过滤， 杀菌 及消毒系统净化为直接饮用水， 净化水量可从家居用水到工商业用的饮用水。
[0007] 为达到上述的目标， 本发明采用的解决方案如下：
[0008] 大气甘露转化系统设备， 它包括空气净化设备部分 1和制水设备部分 2。
[0009] 所述空气净化设备部分 1包括壳体 11、 设置在壳体内的过滤单元， 所述过滤单 元包括过滤网 12、 纤维布层 13、 活性炭网层 14、 驱动电机 15、 孔板 16、 叶轮 17 、 排风口 18、 紫外杀菌灯 19和控制面板 110; 所述壳体 11中下部的左右两侧幵壳 孔， 所述壳体 11内且位于壳孔的前部设置有过滤网 12， 所述过滤网 12的顶端设 置有纤维布层 13、 位于所述纤维布层 13的上方间隔设置有活性炭网 14， 所述过 滤网 12、 纤维布层 13、 活性炭网层 14、 相互平行设置且与壳体 1的内壁固定连接 ， 位于所述活性炭网层 14的上方设置有孔板 16， 所述孔板 16与壳体 1的内壁固定 连接， 所述孔板 16上固定安装有用于驱动叶轮 17的驱动电机 15， 所述驱动电机 1 5的输出轴与叶轮 17连接， 所述壳体 11顶端设置有排风板 18， 位于所述排风板 18 与孔板 16之间壳体 1的内壁上设置有紫外线杀菌灯 19， 位于所述壳体 11的台阶处 的外侧壁上设置有控制面板 110。
[0010] 所述制水设备部分 2包括壳体 21， 机壳上设置控制面版 225、 湿度控制器 22、 空 气通过网 23、 冷凝蒸发器 24、 集水盘 25、 集水箱 26、 集水箱水位控制器 27、 增 压泵 28、 过滤系统 29、 反渗透净化系统 210、 纳米紫外线杀菌消毒器 211、 恒温 净水缸 212、 电解槽 213、 饮用酸水阀 214、 饮用碱水阀 215、 饮用中性水阀 216、 抽风机 217、 压缩机 220、 排风板 223、 负氧离子发生器 226、 自来水或不能饮用 水源入口 227。
[0011] 所述的空气净化设备部分 1与制水设备部分 2通过管道 00连接， 所述管道 00连接 在所述排风板 18和空气通过网 23之间。
[0012] 所述大气甘露转化系统设备的工作原理是， 通过驱动电机 15控制叶轮 17旋转， 空气从壳孔进入壳体 11内部， 则过滤网 12、 纤维布层 13、 活性炭网 14依次对空 气进行处理， 经过处理后的空气穿过孔板 16再通过紫外线杀菌灯 19对空气进行 杀菌， 由排风板 18将经过净化后的空气由管道 00排出至空气通过网 23， 由湿度 控制调节器 22、 抽风机 17、 冷凝蒸发器 24、 压缩机 220组成的空气抽取水份系统 ， 由冷凝蒸发器 24把空气降温至露点的温度； 在露点的温度下空气的水份便被 提取凝结成水珠， 水珠便从冷凝蒸发器自动滴到集水盘 25上， 集水盘 25把水收 集到集水箱 26， 集水箱 26根据水位控制器 27控制连接集水箱的增压泵 28把水增 压， 水到过滤系统 29把一般的微小杂质清除； 再通过反渗透净化系统 210， 通过 吸附、 超滤、 超纯化把溶解在水中的绝大部分无机盐 (包重金属）、 有机物、 细菌 及病毒分隔， 把水质直接转化为超纯水； 超纯水再连接到接纳米紫外线杀菌消 毒器 211， 再次净化后储存到净水缸， 净水箱内置水位显示器及底部分别连接饮 用中性水阀 16和电解槽 213， 供使用者选择放出中性水或者通过电解槽 213， 由 饮用酸水阀 214、 饮用碱水阀 215放出酸水或碱水。 经制水设备部分 2的湿度控制 调节器 22、 抽风机 17、 冷凝蒸发器 24、 压缩机 220组成的空气抽取水份系统后的 净化和除湿空气， 由冷凝蒸发器 24通过负氧离子发生器 226后经排风板 223排出
[0013] 由湿度控制器控制器 22控制从所述空气净化设备部分 1的排风板 18排放的初步 处理的空气湿度是否足够提出空气中的水份， 若空气湿度过低， 低于 38%， 则抽 风机 17、 冷凝蒸发器 24、 压缩机 220组成的空气抽取水份系统抽取水分功能便停 止运作， 而仅使用其调节空气温度的功能； 而由自来水或未达饮用标准的水源 227通过大气甘露转化系统设备中增加泵 28， 连接过滤系统 29、 反渗透净化系统 210和纳米紫外线杀菌消毒器 211。 所述大气甘露转化系统设备的空气净化设备 部分 1， 与室外连接， 处理从室外抽入的空气， 通过制水设备部分 2向室内排放 经过净化和增加负氧离子的优质空气。
[0014] 自来水或未达饮用标准的水源 227可经外置初级过滤器处理， 如水源比较差的 情况需要增加颗粒炭滤芯过滤器及活性炭过滤器， 过滤水中染质， 再接到大气 甘露转化系统制水机的增压泵 28。
发明的有益效果
有益效果
[0015] 本大气甘露转化系统设备可以通过空气净化设备部分 1过滤空气中的灰尘、 烟 尘、 粉尘、 棉绒、 动物毛屑、 螨虫、 花粉、 霉菌孢子和带菌微粒等， 通过制水 设备部分 2控制空气湿度和增加负氧离子， 向室内排放洁净空气， 并且同吋可以 起到调节空气温度的功能； 而制水设备部分 2可以制得优质、 清洁、 无菌、 无毒 害、 酸碱中性水三合一的饮用水， 本大气甘露转化系统设备集成了空调、 空气 净化器、 纯净水机和酸碱水机的功能于一体， 是一种更为具备优势的设备。
[0016] 以上所述， 仅是本发明的较佳实施例， 并非对本发明作任何限制， 凡是根据本 发明技术实质对以上实施例所作的任何简单修改、 变更以及等效结构变化， 均 仍属于本发明技术方案的保护范围内。
对附图的简要说明
附图说明
[0017] 图 1为大气甘露转化系统设备示意图。
[0018] 1为空气净化设备部分； 2为制水设备部分； 所述的空气净化设备部分 1与制水 设备部分 2通过管道 00连接。
[0019] 图 2为空气净化设备部分示意图。
[0020] 图 3-1为制水设备部分正面示意图
[0021] 图 3-2为制水设备部分内部结构示意图
[0022] 图 3-3制水设备部分背面示意图
[0023] 图 4为冷凝蒸发器 24的工作原理图
[0024] 图 5为反渗透净化系统 210工作流程及原理图
[0025] 反渗透膜系統主要工作的原理是它采用反渗透膜技术。 它的工作原理是对水施 加一定的压力， 使水分子和离子态的矿物质元素通过反渗透膜， 而溶解在水中 的绝大部分无机盐 (包括重金属)， 有机物以及细菌、 病毒等无法透过反渗透膜， 从而使渗透过的纯净水和无法渗透过的浓缩水严格的分幵；
[0026] 反渗透膜上的孔径只有 0.0001微米， 而病毒的直径一般有 0.02-0.4微米， 普通 细菌的直径有 0.4-1微米， 所以你尽可以放心大胆的饮用纯水机里流出的清泉。
[0027] 图 6为纳米紫外线杀菌消毒器 211工作原理图
[0028] 纳米紫外线消毒器筒体用不锈钢制造， 内壁多作抛光处理以提高对紫外线的反 射能力和增强辐射强度， 还可根据处理水量的大小调整紫外灯的数量。 有的消 毒器在筒体内壁加装了螺旋形叶片以改变水流的运动状态而避免出现死水和管 道堵塞， 所产生的紊流以及叶片锋利的边缘会打碎悬浮固体， 使附着的微生物 完全暴露于紫外线的辐射中， 提高了消毒效率。
[0029] 纳米紫外线杀菌消毒器的消毒原理， 从紫外线杀菌主要是利用 254纳米波长的 紫外线光。 此波长的紫外线光， 即使是在微量的紫外线投射剂量下， 也可以破 坏一个细胞的生命核心一 DNA， 因此阻止细胞再生,丧失再生能力使细菌变得 无害， 从而达到灭菌的效果。 象所有其它紫外线应用技术一样， 这种系统的规 模取决于紫外线的强度 （照射器的强度和功率） 和接触吋间 （水、 液体、 或空 气暴露在紫外线下的吋间长短） 。
[0030] 图 7为负氧离子发生器 26的工作原理示意图
[0031] 负离子发生器 26由壳体 30， 以及固定安装在该壳体内表面覆盖纳米二氧化钛的 泡沫镍网第一电极 34、 纱布绝缘层 35、 不锈钢网第二电极 36、 电压转换电路 32 组成。 所述第一电极 34、 纱布绝缘层 35和第二电极 36紧贴安装， 组成具有电容 特性的组件 37。 所述组件 37与壳体 30在安装固定的接触面处紧密接触， 防止漏 气。 壳体 30上设有空气进口 31和空气出口 33。 空气从空气进口 31流入， 依次流 经第一电极 34、 纱布绝缘层 35、 第二电极 36， 从空气出口 33流出。 所述氧负离 子发生器由 12V蓄电池 (图中未画出)供电。 该负氧离子发生器的作用原理是： 空 气由空气进口 31进入负氧离子发生器的内部， 其中的氧气与所述第一电极 34接 触吋发生氧化还原反应， 产生氧负离子， 氧负离子随气流从空气出口 33流出。
[0032] 图 8为大气甘露转化系统设备工作流程图。 本发明的实施方式
[0033] 实施例 1
[0034] 空气湿度过高吋大气甘露转化系统设备的工作
[0035] 通过驱动电机 15控制叶轮 17旋转， 空气从壳孔进入壳体 11内部， 则过滤网 12、 纤维布层 13、 活性炭网 14依次对空气进行处理， 经过处理后的空气穿过孔板 16 再通过紫外线杀菌灯 19对空气进行杀菌， 由排风板 18将经过净化后的空气由管 道 00排出至空气通过网 23。
[0036] 湿度控制调节器 22检测， 从空气通过网 23中进入的空气湿度高于 55%， 湿度为 65% , 由湿度控制调节器 22、 抽风机 17、 冷凝蒸发器 24、 压缩机 220组成的空气 抽取水份系统幵始工作， 由冷凝蒸发器 24把空气降温至露点的温度； 在露点的 温度下空气的水份便被提取凝结成水珠， 水珠便从冷凝蒸发器自动滴到集水盘 2 5上， 集水盘 25把水收集到集水箱 26， 集水箱 26根据水位控制器 27控制连接集 水箱的增压泵 28把水增压， 水到过滤系统 29把一般的微小杂质清除； 再通过反 渗透净化系统 210， 通过吸附、 超滤、 超纯化把溶解在水中的绝大部分无机盐（ 包重金属）、 有机物、 细菌及病毒分隔， 把水质直接转化为超纯水； 超纯水再连 接到接纳米紫外线杀菌消毒器 211， 再次净化后储存到净水缸， 净水箱内置水位 显示器及底部分别连接饮用中性水阀 16和电解槽 213， 供使用者选择放出中性水 或者通过电解槽 213， 由饮用酸水阀 214、 饮用碱水阀 215放出酸水或碱水。 经制 水设备部分 2的湿度控制调节器 22、 抽风机 17、 冷凝蒸发器 24、 压缩机 220组成 的空气抽取水份系统后的净化和除湿空气， 通过负氧离子发生器 226后经排风板 223排出。
[0037] 实施例 2
[0038] 空气湿度正常或过低吋大气甘露转化系统设备的工作
[0039] 通过驱动电机 15控制叶轮 17旋转， 空气从壳孔进入壳体 11内部， 则过滤网 12、 纤维布层 13、 活性炭网 14依次对空气进行处理， 经过处理后的空气穿过孔板 16 再通过紫外线杀菌灯 19对空气进行杀菌， 由排风板 18将经过净化后的空气由管 道 00排出至空气通过网 23。
[0040] 湿度控制调节器 22检测， 从空气通过网 23中进入的空气湿度低于 38%， 湿度为 35% , 由湿度控制调节器 22、 抽风机 17、 冷凝蒸发器 24、 压缩机 220组成的空气 抽取水份系统停止抽取水分工作， 而改成调节空气的温度， 由冷凝蒸发器 24把 空气降温至合适的温度。
由自来水或未达饮用标准的水源 227通过大气甘露转化系统设备中增压泵 28， 连接过滤系统 29、 反渗透净化系统 210和纳米紫外线杀菌消毒器 211， 再次净化 后储存到净水缸， 净水箱内置水位显示器及底部分别连接饮用中性水阀 16和电 解槽 213， 供使用者选择放出中性水或者通过电解槽 213， 由饮用酸水阀 214、 饮 用碱水阀 215放出酸水或碱水。 经制水设备部分 2的湿度控制调节器 22、 抽风机 1 7、 冷凝蒸发器 24、 压缩机 220组成的空气抽取水份系统后的净化和除湿空气， 通过负氧离子发生器 226后经排风板 223排出。

Claims

权利要求书
[权利要求 1] 一种大气甘露转化系统设备， 所述大气甘露转化系统设备包括空气净 化设备部分 1和制水设备部分 2;
所述空气净化设备部分 1包括壳体 11、 设置在壳体内的过滤单元， 所 述过滤单元包括过滤网 12、 纤维布层 13、 活性炭网层 14、 驱动电机 15 、 孔板 16、 叶轮 17、 排风口 18、 紫外杀菌灯 19和控制面板 110; 所述 壳体 11中下部的左右两侧幵壳孔， 所述壳体 11内且位于壳孔的前部设 置有过滤网 12， 所述过滤网 12的顶端设置有纤维布层 13、 位于所述纤 维布层 13的上方间隔设置有活性炭网 14， 所述过滤网 12、 纤维布层 13 、 活性炭网层 14、 相互平行设置且与壳体 1的内壁固定连接， 位于所 述活性炭网层 14的上方设置有孔板 16， 所述孔板 16与壳体 1的内壁固 定连接， 所述孔板 16上固定安装有用于驱动叶轮 17的驱动电机 15， 所 述驱动电机 15的输出轴与叶轮 17连接， 所述壳体 11顶端设置有排风板 18， 位于所述排风板 18与孔板 16之间壳体 1的内壁上设置有紫外线杀 菌灯 19， 位于所述壳体 11的台阶处的外侧壁上设置有控制面板 110;
(1) 所述制水设备部分 2包括壳体 21， 机壳上设置控制面版 225、 湿 度控制器 22、 空气通过网 23、 冷凝蒸发器 24、 集水盘 25、 集水箱 26、 集水箱水位控制器 27、 增压泵 28、 过滤系统 29、 反渗透净化系统 210 、 纳米紫外线杀菌消毒器 211、 恒温净水缸 212、 电解槽 213、 饮用酸 水阀 214、 饮用碱水阀 215、 饮用中性水阀 216、 抽风机 217、 压缩机 22 0、 排风板 223、 负氧离子发生器 226、 自来水或不能饮用水源入口 227 所述的空气净化设备部分 1与制水设备部分 2通过管道 00连接， 所述管 道 00连接在所述排风板 18和空气通过网 23之间；
(2) 所述大气甘露转化系统设备的工作原理是， 通过驱动电机 15控 制叶轮 17旋转， 空气从壳孔进入壳体 11内部， 则过滤网 12、 纤维布层 13、 活性炭网 14依次对空气进行处理， 经过处理后的空气穿过孔板 16 再通过紫外线杀菌灯 19对空气进行杀菌， 由排风板 18将经过净化后的 空气由管道 00排出至空气通过网 23；
(3) 由湿度控制调节器 22、 抽风机 17、 冷凝蒸发器 24、 压缩机 220组 成的空气抽取水份系统， 由冷凝蒸发器 24把空气降温至露点的温度； 在露点的温度下空气的水份便被提取凝结成水珠， 水珠便从冷凝蒸发 器自动滴到集水盘 25上；
(4) 集水盘 25把水收集到集水箱 26， 集水箱 26根据水位控制器 27控 制连接集水箱的增压泵 28把水增压， 水经过滤系统 29、 反渗透净化系 统 210、 纳米紫外线杀菌消毒器
211， 再次净化后储存到恒温净水缸 212;
(5) 净水箱内置水位显示器及底部分别连接饮用中性水阀 216和电解 槽 213， 供使用者选择放出中性水或者通过电解槽 213， 由饮用酸水阀 214、 饮用碱水阀 215放出酸水或碱水； 经制水设备部分 2的湿度控制 调节器 22、 抽风机 17、 冷凝蒸发器 24、 压缩机 220组成的空气抽取水 份系统后的净化和除湿空气， 由冷凝蒸发器 24通过负氧离子发生器 22 6后经排风板 223排出。
[权利要求 2] 如权利要求 1所述的大气甘露转化系统设备， 其特征在于所述设备还 包括自来水或未达饮用标准的水源 227， 当湿度控制器控制器 22检测 湿度低于 38%， 由所述自来水或未达饮用标准的水源 227通过大气甘 露转化系统设备中增加泵 28， 连接过滤系统 29、 反渗透净化系统 210 和纳米紫外线杀菌消毒器 211。
[权利要求 3] 如权利要求 1或 2所述的大气甘露转化系统设备， 其特征在于所述的负 离子发生器 26由壳体 30， 以及固定安装在该壳体内表面覆盖纳米二氧 化钛的泡沫镍网第一电极 34、 纱布绝缘层 35、 不锈钢网第二电极 36、 电压转换电路 32组成。 所述第一电极 34、 纱布绝缘层 35和第二电极 36 紧贴安装， 组成具有电容特性的组件 37。 所述组件 37与壳体 30在安装 固定的接触面处紧密接触， 防止漏气。 壳体 30上设有空气进口 31和空 气出口 33。 空气从空气进口 31流入， 依次流经第一电极 34、 纱布绝缘 层 35、 第二电极 36， 从空气出口 33流出。 所述氧负离子发生器由 12V 蓄电池 (图中未画出)供电。 该负氧离子发生器的作用原理是： 空气由 空气进口 31进入负氧离子发生器的内部， 其中的氧气与所述第一电极 34接触吋发生氧化还原反应， 产生氧负离子， 氧负离子随气流从空气 出口 33流出。
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