WO2017024969A1 - 气体产生器 - Google Patents

气体产生器 Download PDF

Info

Publication number
WO2017024969A1
WO2017024969A1 PCT/CN2016/092990 CN2016092990W WO2017024969A1 WO 2017024969 A1 WO2017024969 A1 WO 2017024969A1 CN 2016092990 W CN2016092990 W CN 2016092990W WO 2017024969 A1 WO2017024969 A1 WO 2017024969A1
Authority
WO
WIPO (PCT)
Prior art keywords
hydrogen
water
mixed gas
condensing
water tank
Prior art date
Application number
PCT/CN2016/092990
Other languages
English (en)
French (fr)
Inventor
林信涌
Original Assignee
林信涌
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 林信涌 filed Critical 林信涌
Priority to SG11201801139TA priority Critical patent/SG11201801139TA/en
Priority to ES16834593T priority patent/ES2923768T3/es
Priority to MYPI2018700490A priority patent/MY189853A/en
Priority to US15/751,017 priority patent/US10869988B2/en
Priority to PL16834593.2T priority patent/PL3336220T3/pl
Priority to KR1020187006467A priority patent/KR102097382B1/ko
Priority to EP16834593.2A priority patent/EP3336220B1/en
Priority to JP2018506556A priority patent/JP6665975B2/ja
Publication of WO2017024969A1 publication Critical patent/WO2017024969A1/zh

Links

Images

Classifications

    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61M—DEVICES FOR INTRODUCING MEDIA INTO, OR ONTO, THE BODY; DEVICES FOR TRANSDUCING BODY MEDIA OR FOR TAKING MEDIA FROM THE BODY; DEVICES FOR PRODUCING OR ENDING SLEEP OR STUPOR
    • A61M16/00—Devices for influencing the respiratory system of patients by gas treatment, e.g. mouth-to-mouth respiration; Tracheal tubes
    • A61M16/10—Preparation of respiratory gases or vapours
    • A61M16/12—Preparation of respiratory gases or vapours by mixing different gases
    • A61M16/122—Preparation of respiratory gases or vapours by mixing different gases with dilution
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B1/00—Electrolytic production of inorganic compounds or non-metals
    • C25B1/01—Products
    • C25B1/02—Hydrogen or oxygen
    • C25B1/04—Hydrogen or oxygen by electrolysis of water
    • C25B1/044—Hydrogen or oxygen by electrolysis of water producing mixed hydrogen and oxygen gas, e.g. Brown's gas [HHO]
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61M—DEVICES FOR INTRODUCING MEDIA INTO, OR ONTO, THE BODY; DEVICES FOR TRANSDUCING BODY MEDIA OR FOR TAKING MEDIA FROM THE BODY; DEVICES FOR PRODUCING OR ENDING SLEEP OR STUPOR
    • A61M16/00—Devices for influencing the respiratory system of patients by gas treatment, e.g. mouth-to-mouth respiration; Tracheal tubes
    • A61M16/021—Devices for influencing the respiratory system of patients by gas treatment, e.g. mouth-to-mouth respiration; Tracheal tubes operated by electrical means
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61M—DEVICES FOR INTRODUCING MEDIA INTO, OR ONTO, THE BODY; DEVICES FOR TRANSDUCING BODY MEDIA OR FOR TAKING MEDIA FROM THE BODY; DEVICES FOR PRODUCING OR ENDING SLEEP OR STUPOR
    • A61M16/00—Devices for influencing the respiratory system of patients by gas treatment, e.g. mouth-to-mouth respiration; Tracheal tubes
    • A61M16/10—Preparation of respiratory gases or vapours
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61M—DEVICES FOR INTRODUCING MEDIA INTO, OR ONTO, THE BODY; DEVICES FOR TRANSDUCING BODY MEDIA OR FOR TAKING MEDIA FROM THE BODY; DEVICES FOR PRODUCING OR ENDING SLEEP OR STUPOR
    • A61M16/00—Devices for influencing the respiratory system of patients by gas treatment, e.g. mouth-to-mouth respiration; Tracheal tubes
    • A61M16/10—Preparation of respiratory gases or vapours
    • A61M16/1005—Preparation of respiratory gases or vapours with O2 features or with parameter measurement
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61M—DEVICES FOR INTRODUCING MEDIA INTO, OR ONTO, THE BODY; DEVICES FOR TRANSDUCING BODY MEDIA OR FOR TAKING MEDIA FROM THE BODY; DEVICES FOR PRODUCING OR ENDING SLEEP OR STUPOR
    • A61M16/00—Devices for influencing the respiratory system of patients by gas treatment, e.g. mouth-to-mouth respiration; Tracheal tubes
    • A61M16/10—Preparation of respiratory gases or vapours
    • A61M16/105—Filters
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61M—DEVICES FOR INTRODUCING MEDIA INTO, OR ONTO, THE BODY; DEVICES FOR TRANSDUCING BODY MEDIA OR FOR TAKING MEDIA FROM THE BODY; DEVICES FOR PRODUCING OR ENDING SLEEP OR STUPOR
    • A61M16/00—Devices for influencing the respiratory system of patients by gas treatment, e.g. mouth-to-mouth respiration; Tracheal tubes
    • A61M16/10—Preparation of respiratory gases or vapours
    • A61M16/12—Preparation of respiratory gases or vapours by mixing different gases
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61M—DEVICES FOR INTRODUCING MEDIA INTO, OR ONTO, THE BODY; DEVICES FOR TRANSDUCING BODY MEDIA OR FOR TAKING MEDIA FROM THE BODY; DEVICES FOR PRODUCING OR ENDING SLEEP OR STUPOR
    • A61M16/00—Devices for influencing the respiratory system of patients by gas treatment, e.g. mouth-to-mouth respiration; Tracheal tubes
    • A61M16/10—Preparation of respiratory gases or vapours
    • A61M16/14—Preparation of respiratory gases or vapours by mixing different fluids, one of them being in a liquid phase
    • A61M16/16—Devices to humidify the respiration air
    • 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
    • B01D53/02—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 by adsorption, e.g. preparative gas chromatography
    • B01D53/04—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 by adsorption, e.g. preparative gas chromatography with stationary adsorbents
    • B01D53/0407—Constructional details of adsorbing systems
    • 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
    • B01D53/26—Drying gases or vapours
    • B01D53/265—Drying gases or vapours by refrigeration (condensation)
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B1/00—Electrolytic production of inorganic compounds or non-metals
    • C25B1/01—Products
    • C25B1/02—Hydrogen or oxygen
    • C25B1/04—Hydrogen or oxygen by electrolysis of water
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B15/00—Operating or servicing cells
    • C25B15/08—Supplying or removing reactants or electrolytes; Regeneration of electrolytes
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B15/00—Operating or servicing cells
    • C25B15/08—Supplying or removing reactants or electrolytes; Regeneration of electrolytes
    • C25B15/085—Removing impurities
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B9/00—Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
    • C25B9/70—Assemblies comprising two or more cells
    • C25B9/73—Assemblies comprising two or more cells of the filter-press type
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61M—DEVICES FOR INTRODUCING MEDIA INTO, OR ONTO, THE BODY; DEVICES FOR TRANSDUCING BODY MEDIA OR FOR TAKING MEDIA FROM THE BODY; DEVICES FOR PRODUCING OR ENDING SLEEP OR STUPOR
    • A61M16/00—Devices for influencing the respiratory system of patients by gas treatment, e.g. mouth-to-mouth respiration; Tracheal tubes
    • A61M16/08—Bellows; Connecting tubes ; Water traps; Patient circuits
    • A61M16/0816—Joints or connectors
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61M—DEVICES FOR INTRODUCING MEDIA INTO, OR ONTO, THE BODY; DEVICES FOR TRANSDUCING BODY MEDIA OR FOR TAKING MEDIA FROM THE BODY; DEVICES FOR PRODUCING OR ENDING SLEEP OR STUPOR
    • A61M16/00—Devices for influencing the respiratory system of patients by gas treatment, e.g. mouth-to-mouth respiration; Tracheal tubes
    • A61M16/08—Bellows; Connecting tubes ; Water traps; Patient circuits
    • A61M16/0875—Connecting tubes
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61M—DEVICES FOR INTRODUCING MEDIA INTO, OR ONTO, THE BODY; DEVICES FOR TRANSDUCING BODY MEDIA OR FOR TAKING MEDIA FROM THE BODY; DEVICES FOR PRODUCING OR ENDING SLEEP OR STUPOR
    • A61M16/00—Devices for influencing the respiratory system of patients by gas treatment, e.g. mouth-to-mouth respiration; Tracheal tubes
    • A61M16/08—Bellows; Connecting tubes ; Water traps; Patient circuits
    • A61M16/0883—Circuit type
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61M—DEVICES FOR INTRODUCING MEDIA INTO, OR ONTO, THE BODY; DEVICES FOR TRANSDUCING BODY MEDIA OR FOR TAKING MEDIA FROM THE BODY; DEVICES FOR PRODUCING OR ENDING SLEEP OR STUPOR
    • A61M16/00—Devices for influencing the respiratory system of patients by gas treatment, e.g. mouth-to-mouth respiration; Tracheal tubes
    • A61M16/20—Valves specially adapted to medical respiratory devices
    • A61M16/208—Non-controlled one-way valves, e.g. exhalation, check, pop-off non-rebreathing valves
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61M—DEVICES FOR INTRODUCING MEDIA INTO, OR ONTO, THE BODY; DEVICES FOR TRANSDUCING BODY MEDIA OR FOR TAKING MEDIA FROM THE BODY; DEVICES FOR PRODUCING OR ENDING SLEEP OR STUPOR
    • A61M16/00—Devices for influencing the respiratory system of patients by gas treatment, e.g. mouth-to-mouth respiration; Tracheal tubes
    • A61M16/20—Valves specially adapted to medical respiratory devices
    • A61M16/208—Non-controlled one-way valves, e.g. exhalation, check, pop-off non-rebreathing valves
    • A61M16/209—Relief valves
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61M—DEVICES FOR INTRODUCING MEDIA INTO, OR ONTO, THE BODY; DEVICES FOR TRANSDUCING BODY MEDIA OR FOR TAKING MEDIA FROM THE BODY; DEVICES FOR PRODUCING OR ENDING SLEEP OR STUPOR
    • A61M2202/00—Special media to be introduced, removed or treated
    • A61M2202/02—Gases
    • A61M2202/0208—Oxygen
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61M—DEVICES FOR INTRODUCING MEDIA INTO, OR ONTO, THE BODY; DEVICES FOR TRANSDUCING BODY MEDIA OR FOR TAKING MEDIA FROM THE BODY; DEVICES FOR PRODUCING OR ENDING SLEEP OR STUPOR
    • A61M2205/00—General characteristics of the apparatus
    • A61M2205/07—General characteristics of the apparatus having air pumping means
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61M—DEVICES FOR INTRODUCING MEDIA INTO, OR ONTO, THE BODY; DEVICES FOR TRANSDUCING BODY MEDIA OR FOR TAKING MEDIA FROM THE BODY; DEVICES FOR PRODUCING OR ENDING SLEEP OR STUPOR
    • A61M2205/00—General characteristics of the apparatus
    • A61M2205/33—Controlling, regulating or measuring
    • A61M2205/3331—Pressure; Flow
    • A61M2205/3334—Measuring or controlling the flow rate
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61M—DEVICES FOR INTRODUCING MEDIA INTO, OR ONTO, THE BODY; DEVICES FOR TRANSDUCING BODY MEDIA OR FOR TAKING MEDIA FROM THE BODY; DEVICES FOR PRODUCING OR ENDING SLEEP OR STUPOR
    • A61M2205/00—General characteristics of the apparatus
    • A61M2205/33—Controlling, regulating or measuring
    • A61M2205/3379—Masses, volumes, levels of fluids in reservoirs, flow rates
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61M—DEVICES FOR INTRODUCING MEDIA INTO, OR ONTO, THE BODY; DEVICES FOR TRANSDUCING BODY MEDIA OR FOR TAKING MEDIA FROM THE BODY; DEVICES FOR PRODUCING OR ENDING SLEEP OR STUPOR
    • A61M2205/00—General characteristics of the apparatus
    • A61M2205/36—General characteristics of the apparatus related to heating or cooling
    • A61M2205/3606—General characteristics of the apparatus related to heating or cooling cooled
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61M—DEVICES FOR INTRODUCING MEDIA INTO, OR ONTO, THE BODY; DEVICES FOR TRANSDUCING BODY MEDIA OR FOR TAKING MEDIA FROM THE BODY; DEVICES FOR PRODUCING OR ENDING SLEEP OR STUPOR
    • A61M2205/00—General characteristics of the apparatus
    • A61M2205/75—General characteristics of the apparatus with filters
    • A61M2205/7536—General characteristics of the apparatus with filters allowing gas passage, but preventing liquid passage, e.g. liquophobic, hydrophobic, water-repellent membranes
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61M—DEVICES FOR INTRODUCING MEDIA INTO, OR ONTO, THE BODY; DEVICES FOR TRANSDUCING BODY MEDIA OR FOR TAKING MEDIA FROM THE BODY; DEVICES FOR PRODUCING OR ENDING SLEEP OR STUPOR
    • A61M2205/00—General characteristics of the apparatus
    • A61M2205/82—Internal energy supply devices
    • A61M2205/8218—Gas operated
    • A61M2205/8231—Gas operated using electrochemical gas generating device for the driving gas
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61M—DEVICES FOR INTRODUCING MEDIA INTO, OR ONTO, THE BODY; DEVICES FOR TRANSDUCING BODY MEDIA OR FOR TAKING MEDIA FROM THE BODY; DEVICES FOR PRODUCING OR ENDING SLEEP OR STUPOR
    • A61M2209/00—Ancillary equipment
    • A61M2209/08—Supports for equipment
    • A61M2209/084—Supporting bases, stands for equipment
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
    • B01D2253/10—Inorganic adsorbents
    • B01D2253/102—Carbon
    • 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
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30—Hydrogen technology
    • Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis

Definitions

  • This invention relates to a gas generator, and more particularly to a gas generator having a filtering, humidifying function and reducing electrolyte consumption.
  • the hydrogen-oxygen mixed gas produced after electrolytically electrolyzing water through an electrolysis device generally has a relatively high temperature and is relatively dry, and is not suitable for direct inhalation by a human body.
  • the above problems in turn, often cause inconvenience in the use of conventional electrolyzers.
  • a gas generator for use in an electrolyte state water to produce a hydrogen-oxygen mixed gas, followed by condensation and filtration of an electrolyte of a hydrogen-oxygen mixed gas, followed by humidification and lower gas containing electrolyte.
  • the supplemental water is replenished and the electrolyte is backflushed to the electrolysis device to restore the filtration capacity of the circulation flow path, prevent clogging and corrosion of the circulation flow path, and reduce electrolyte consumption.
  • the present invention discloses a gas generator characterized by comprising:
  • a water tank containing electrolyzed water, the electrolyzed water containing an electrolyte
  • An electrolysis device is disposed in the water tank for electrolyzing the electrolyzed water to generate a hydrogen-oxygen mixed gas
  • a condensing filter is connected to the electrolysis device for condensing the hydrogen-oxygen mixed gas generated by the electrolysis device and filtering the electrolyte in the hydrogen-oxygen mixed gas to generate the filtered hydrogen-oxygen mixed gas;
  • a humidifying device which accommodates a supplementary water and is connected to the condensing filter for humidifying the filtered mixed gas of hydrogen and oxygen;
  • a water pump device connected to the water tank for generating a negative pressure in the water tank, whereby the makeup water is pumped back from the humidification device via the condensing filter to be input to the water tank, and adsorbed to the condensing filter
  • the electrolyte inside is backflushed to the water tank;
  • the loss of the electrolyte is less than 3 to 5 grams.
  • the electrolyte is food grade sodium hydroxide.
  • the method further includes an atomization/volatile gas mixing tank, wherein the atomization/volatile gas mixing tank comprises an air outlet, and the water tank and the atomization/volatile gas mixing tank are connected to each other by the water pump device, and the water pump device During operation, the gas inside the water tank is withdrawn and discharged from the air outlet of the atomizing/volatile gas mixing tank to generate the negative pressure in the water tank.
  • the atomization/volatile gas mixing tank is connected to the humidification device to receive the humidified hydrogen-oxygen mixed gas, and the atomization/volatile gas mixing tank generates an atomizing gas and the humidified hydrogen-oxygen mixed gas.
  • the humidification device further includes at least one output tube, the at least one output tube has a plurality of perforations, and the hydrogen-oxygen mixed gas is discharged through the plurality of perforations of the at least one output tube to humidify the filtered hydrogen and oxygen mixed composition.
  • the condensing filter comprises a plurality of condensing sheets, each condensing sheet has a first-class trajectory, and the flow passage of the condensing sheet communicates with the adjacent flow passage of the condensing sheet, thereby forming a circulation of the oxyhydrogen mixed gas a circular flow path.
  • the flow channel is composed of a diverging flow channel and a communication flow channel, the diverging flow channel of the condensing sheet and the diverging flow channel of the adjacent condensing sheet by the condensing sheet
  • the communication channels are connected to each other.
  • the flow channel is provided with an activated carbon fiber to filter the impurity in the hydrogen-oxygen mixed gas, and the impurity is an electrolyte in the electrolyzed water.
  • the flow channel is further provided with any filter material composed of ceramic, quartz stone, diatomaceous earth, sepiolite or a combination of the above materials.
  • the diverging flow channel is a cross-sectionally expanding flow channel, and the diverging flow channel includes an opening having a first-class channel and two corresponding openings, and the two corresponding channels of the connecting channel Opening by the flow
  • the passages are interconnected, the opening of the divergent flow passage of the condensing sheet and the opening of the divergent flow passage of the adjacent condensing sheet corresponding to the two of the communicating flow passages of the condensing sheet
  • the openings are connected to each other.
  • a water tank containing an electrolyzed water, the electrolyzed water comprising an electrolyte
  • An electrolysis device is disposed in the water tank for electrolyzing the electrolyzed water to generate a hydrogen-oxygen mixed gas
  • a condensing filter is connected to the electrolysis device for condensing the hydrogen-oxygen mixed gas generated by the electrolysis device and filtering the electrolyte in the hydrogen-oxygen mixed gas to generate the filtered hydrogen-oxygen mixed gas;
  • a humidifying filter which is filled with water and connected to the condensing filter for filtering the hydrogen-oxygen mixed gas filtered by the condensing filter;
  • a humidifying device which accommodates a makeup water and is connected to the humidification filter for humidifying the hydrogen-oxygen mixed gas filtered through the humidification filter;
  • a water pump device connected to the water tank for generating a negative pressure in the water tank, whereby the makeup water is pumped back to the water tank by the humidification device via the humidification filter and the condensing filter, and The electrolyte adsorbed in the condensing filter is backflushed to the water tank;
  • the loss of the electrolyte is less than 3 to 5 grams.
  • the present invention is directed to a gas generator in which a hydrogen-oxygen mixed gas produced by an electrolysis device can be first condensed by a condensing filter and filtered, and then the electrolyte is filtered.
  • the humidification device is used to humidify and the gas contains a lower amount of electrolyte to provide a mixed gas of hydrogen and oxygen suitable for human inhalation.
  • a humidification filter between the condensing filter and the humidifying device may be further included, which may again filter impurities in the hydrogen-oxygen mixed gas to provide a hydrogen-oxygen mixed gas more suitable for human body inhalation.
  • the design of the present invention can be used to supplement the makeup water and backflush the electrolyte to the electrolysis device to restore the filtration capacity of the circulation flow path, prevent clogging and corrosion of the circulation flow path, and reduce electrolyte consumption.
  • FIG. 1A and 1B are schematic views showing different angles of view of a gas generator of the present invention in an embodiment.
  • FIGS. 2A, 2B, and 2C are schematic views showing different angles of view of the gas generator of the present invention in one embodiment.
  • 3A, 3B, and 3C are schematic views showing different angles of the outer casing without the water tank, the upper cover of the water tank, the frame of the humidifier, and the outer tube of the humidifier in the embodiment shown in FIG. 2A.
  • FIG. 3A and 4B are schematic views showing different perspectives of the embodiment shown in FIG. 3A without a water tank.
  • 5A and 5B are plan views showing only the condensing filter and the water tank cover in the embodiment shown in Fig. 2A, and a cross-sectional view taken along line A-A of the plan view.
  • 6A and 6B are schematic views showing different angles of view when the gas generator of the present invention has only a combination of a condensing filter and a tank cover in another embodiment.
  • Figure 7 is a schematic view showing the embodiment of Figure 6 without the water tank cover.
  • Figure 8 is a schematic view showing the embodiment of Figure 7 without a filter.
  • Figure 9 is a schematic view showing the embodiment of Figure 8 without the filter cover.
  • FIGS. 10A and 10B are plan views showing the condensing filter of the gas generator of the present invention in the embodiment shown in Fig. 6A and a cross-sectional view taken along line B-B of the plan view.
  • Figure 11 is a schematic view showing the humidification device of the gas generator of the present invention in another embodiment.
  • Figure 12 is a schematic view showing another embodiment of the gas generator of the present invention.
  • FIG. 1A and FIG. 1B are schematic diagrams showing different angles of view of the gas generator of the present invention in one embodiment
  • FIGS. 2A, 2B and 2C are diagrams showing the gas of the present invention
  • FIG. 3A, FIG. 3B and FIG. 3C are diagrams showing the outer casing without the water tank, the upper cover of the water tank, the frame of the humidifier, and the frame of the humidifier according to the embodiment shown in FIG. 2A.
  • the gas generator 1 of the present invention comprises a water tank 2, an electrolysis device 3 (not shown in Figs. 1A and 1B, which are shown in Figs.
  • FIGS. 1A and 1B which are shown in FIGS. 2B to 4B
  • a condensing filter 6 a cooling device 7, and a humidifying device 9.
  • the water tank 2 houses electrolyzed water, wherein the electrolyzed water contains an electrolyte.
  • the electrolysis device 3 is disposed in the water tank 2 for electrolytically electrolyzing water to produce a hydrogen-oxygen mixed gas.
  • the condensing filter 6 is in communication with the electrolysis device 3 for receiving and condensing the hydrogen-oxygen mixed gas generated by the electrolysis device 3, and filtering the electrolyte in the hydrogen-oxygen mixed gas to produce a filtered hydrogen-oxygen mixed gas.
  • the humidification device 9 is for receiving and humidifying the filtered hydrogen-oxygen mixed gas.
  • the humidifying device 9 houses a supplementary water and communicates with the first hollow portion 20 of the water tank 2.
  • the water pump device 5 communicates with the first hollow portion 20 of the water tank 2.
  • the water pump device 5 extracts the gas inside the first hollow portion 20 of the water tank 2 to cause a negative pressure inside the water tank 2.
  • the humidification device 9 backwashes the makeup water back to the condensing filter 6 by a negative pressure and replenishes the input into the water tank 2 to reduce the loss of the electrolyte.
  • the flow rate of the mixed gas of hydrogen and oxygen is 120 liters per hour.
  • the loss of electrolyte is less than or equal to 50 grams; it can also be estimated as when the gas generator generates a mixture of hydrogen and oxygen.
  • the flow rate is 600 liters per hour and shipped After 40 to 60 hours, the loss of electrolyte is less than or equal to 5 grams.
  • the cooling device 7 is disposed on the lid of the water tank 2 and communicates with the water tank, and can be used to cool the electrolyzed water after the hydrogen-oxygen mixed gas is generated. The design of each component of the present invention will be separately described below.
  • FIG. 5A and FIG. 5B are cross-sectional views of the embodiment of FIG. 6A and 6B are schematic views showing different angles of view when the gas generator of the present invention has only a combination of a condensing filter and a water tank cover in another embodiment.
  • the water tank 2 has a first hollow portion 20.
  • the first hollow portion 20 of the water tank 2 is adapted to contain an electrolyzed water.
  • the electrolyzed water contains an electrolyte which is sodium hydroxide. However, it is not limited to this. In practical applications, the electrolyte may be calcium carbonate, sodium chloride, etc., or even food grade sodium hydroxide.
  • the water tank 2 further includes a duct 22, a tank body 24 and a tank cover 26.
  • the space inside the water tank body 24 is the first hollow portion 20.
  • the duct 22 is disposed in the tank cover 26 to communicate the condensing filter 6 and the water tank 2 for outputting the hydrogen-oxygen mixed gas generated by the electrolysis device 3 and replenishing the input electrolyzed water into the water tank 2.
  • the water tank cover 26 may include a plurality of cover holes communicating with the first hollow portion 20 of the water tank 2 for conducting the electrode column 33 (shown in FIG. 4A) of the power supply device 3 to set the electrolysis device 3 It is placed on the water tank or used for detecting devices (such as flow detectors, water level gauges, safety valves).
  • FIG. 4A and FIG. 4B are schematic diagrams showing different viewing angles of the embodiment shown in FIG. 3A without a water tank.
  • the electrolysis device 3 includes an electrolytic cell body 32, a plurality of electrodes (not shown), a backing plate 36, an upper cover 37, and a lower cover 38.
  • a plurality of electrodes may be disposed in the electrolytic cell body 32 at intervals and form a plurality of electrode flow channels.
  • the bottom of the cell body can have a plurality of lower perforations.
  • a backing plate 36 is provided on the upper surface of each of the electrodes.
  • the backing plate can have a plurality of upper perforations.
  • the upper cover 37 is covered on the other end of the backing plate 36 with respect to the electrolytic cell body 32.
  • the upper cover 37 may have at least one first flow path 370.
  • the plurality of upper perforations located in the backing plate 36 and the first hollow portion 20 are in communication with each other by at least one first flow path 370 of the upper cover 37.
  • the lower cover 38 is disposed on the lower surface of the electrolytic cell body 32 with respect to the other end of the upper cover 37.
  • the lower cover 38 includes at least one second flow path 380.
  • the plurality of lower perforations located at the bottom of the electrolytic cell body 32 and the first hollow portion 20 are in communication with each other by at least one second flow path 380 of the lower cover 38.
  • FIG. 7 is a schematic diagram showing the embodiment of FIG. 6 without the water tank cover.
  • FIG. 8 is a schematic view showing the embodiment of FIG. 7 without a filter.
  • FIG. 9 is a schematic view showing the embodiment of FIG. 8 without the filter cover.
  • 10A and 10B are plan views of the embodiment of the condensing filter of the gas generator of the present invention shown in Fig. 6A and a cross-sectional view taken along line B-B of the plan view.
  • the condensing filter 6 has an air inlet 60 and an air outlet 62.
  • the air inlet 60 is connected to the electrolysis device 3 for receiving the hydrogen-oxygen mixed gas.
  • the air outlet 62 is for discharging the filtered hydrogen-oxygen mixed gas.
  • the condensing filter 6 of the present invention includes a plurality of condensing sheets 64.
  • Each of the condensing fins 64 has a flow path 640a, and the flow path 640a of the condensing sheet 64 communicates with the flow path 640a of the adjacent condensing sheet 64 to form a circulation flow path 640 through which the hydrogen-oxygen mixed gas flows to condense hydrogen. Oxygen mixed gas.
  • the air inlet 60 and the air outlet 62 are provided by the circulation flow path 640. Connected to each other.
  • the flow path 640a of the condensing sheet 64 is composed of a diverging flow path 642 and a communication flow path 644.
  • the diverging flow channel 642 is a flow path which is gradually enlarged in cross section, but is not limited to the diverging flow channel 642 shown in FIG. 5B and FIG. 10B.
  • the cross section of the expanded flow channel is semicircular, triangular or trapezoidal.
  • the tapered flow channel 642 has a relatively wide end and a relatively narrow end.
  • the relatively wide end and the relatively narrow end of the diverging flow passage 642 have an opening.
  • the connecting flow path 644 has a first-class track and two corresponding openings.
  • the two corresponding openings of the communication flow path 644 are connected to each other by the flow path.
  • the diverging flow path 642 and the communication flow path 644 are connected and connected by the opening of the relatively wide end of the diverging flow path 642.
  • the connections of the openings of the flow passages 644 are in communication with each other.
  • the structural design of the flow passage 640a of the condensing fin 64 allows the horizontal flow passage (i.e., the diverging flow passage 642) and the vertical flow passage (i.e., the communication flow passage 644) to communicate with each other, but the horizontal flow passage is not tapered in cross section. The flow channel is limited.
  • the horizontal flow channel can also be a flow channel with the same cross section. Further, when the flow path 640a of the condensing sheet 64 and the flow path 640a of the adjacent condensing sheet 64 are connected to each other, the flow path 640a of the condensing sheet 64 and the flow path 640a of the adjacent condensing sheet 64 are gradually formed by the condensing sheet 64. The connection of the opening at the relatively narrow end of the expanded flow passage 642 and the opening of the communication flow passage 644 of the adjacent condensing fin 64 are in communication with each other.
  • the flow path 640a of the condensing sheet 64 is designed such that the flow path 640a of the condensing sheet 64 and the flow path 640a of the adjacent condensing sheet 64 are in communication with each other, thereby forming a circulation flow path 640 through which the hydrogen-oxygen mixed gas flows. That is to say, in the embodiment, the connection mode of the condensing sheet and the adjacent condensing sheet can drive the hydrogen-oxygen mixed gas to pass through a long condensation and filtration path, thereby achieving better condensation and filtration effects. Further, in an embodiment, an active carbon fiber is disposed in the flow channel 640a for filtering the electrolyte in the hydrogen-oxygen mixed gas.
  • the flow path 640a is additionally provided with any filter material composed of ceramic, quartz stone, diatomaceous earth, sepiolite or a combination of the above, and the filter material can further filter the electrolyte in the hydrogen-oxygen mixed gas.
  • the air inlet 60 of the present invention is composed of a filter 600 and a filter cover 602. The filter 600 and the filter cover 602 are connected to the electrolysis device 3 for receiving the hydrogen-oxygen mixed gas and initially filtering the hydrogen-oxygen mixed gas.
  • the circulation flow path 640 can be composed of two sets of flow channels 640a to achieve the condensing effect, and at the same time, the design of the condensing filter 6 can be simplified and the cost can be reduced. This is limited to the number of runners that can be adjusted according to the designer's needs.
  • FIG. 11 is a schematic diagram showing the humidification device of the gas generator of the present invention in another embodiment.
  • the humidification device 9 of the present invention comprises a hollow body 90, a second conduit 92, at least one output tube 94, a third conduit 96 and a fourth conduit 98.
  • the hollow body 90 is configured to receive a supplemental water.
  • the second conduit 92 is disposed on the hollow body 90 for communication with the electrolysis device 3 (not shown).
  • At least one output tube 94 is disposed in the hollow body 90 and coupled to the second conduit 92.
  • the second conduit 92 is connected to the two output tubes 94 to form a T-shaped structure, but not limited thereto. In practical applications, the connection between the second conduit and the at least one output tube 94 is adjusted depending on the use.
  • the surfaces of the two output tubes 94 each have a plurality of perforations.
  • the perforation has a nanometer pore size ranging from 2 nm to 10 nm for refining the gas to form a resolvable refining bubble, but not limited thereto.
  • the aperture size of the perforation is adjusted according to the needs of the user.
  • the ends of the two output tubes 94 connected to the second conduit 92 are respectively provided with rubber stoppers for allowing the hydrogen-oxygen mixed gas received by the second conduit 92 to be perforated by a plurality of nanometers of the two output tubes 94 (not shown in The drawing is discharged to the hollow body 90, but not limited thereto.
  • the ends of the two output tubes 94 connecting the second conduits 92 may also be of a closed design.
  • the third conduit 96 is disposed on the hollow body 90 to supplement the input makeup water W2.
  • the third conduit is connected to a guide hole, and the third conduit passes through the guide hole to pour out hydrogen water or pour in makeup water.
  • the fourth conduit 98 is disposed on the hollow body 90 for outputting the humidified hydrogen-oxygen mixed gas.
  • the water pump device 5 is disposed on the water tank cover 26 and communicates with the first hollow portion 20 of the water tank 2 for extracting gas inside the water tank 2 to generate a negative pressure inside thereof, thereby inputting the supplementary water from the humidification device 9.
  • the electrolyte adsorbed in the condensing filter 6 is backflushed to the first hollow portion 20 of the water tank 2.
  • the atomization/volatile gas mixing tank 4 can be connected to the humidification device 9 to receive the humidified hydrogen-oxygen mixed gas.
  • the atomizing/volatile gas mixing tank can generate an atomizing gas, wherein the atomizing gas is selected from one of a group consisting of water vapor, atomized syrup, volatile essential oil, and combinations thereof.
  • the atomization/volatile gas mixing tank can mix the atomizing gas generated by it with the humidified hydrogen-oxygen mixed gas to form a health care gas for the user to inhale.
  • the atomization/volatile gas mixing tank 4 may include an air outlet 40, but the design of the air outlet is not limited to that shown in FIG. 4A.
  • the air outlet may also be an air outlet, an air outlet, and the like. Can be adjusted according to the needs of users.
  • the air outlet 40 of the atomizing/volatile gas mixing tank 4 communicates with the water pump device 5.
  • the water pump device when the electrolysis device 3 suspends the electrolytic electrolysis water to generate a hydrogen-oxygen mixed gas, the water pump device is activated to operate, and the water pump device 5 can extract the gas inside the water tank and is mixed by the atomization/volatile gas mixing tank 4.
  • the air outlet 40 is exhausted to generate a negative pressure in the water tank, whereby the makeup water is input from the humidification device to the water tank, and the electrolyte adsorbed in the condensing filter is backflushed to the water tank.
  • a plurality of electrodes are respectively disposed at the electrolytic cell body 32, the backing plate 36 is disposed on the upper surface of each electrode, and the upper cover 37 is disposed on the backing plate 36 with respect to the electrolytic cell body 32.
  • the lower cover 38 is disposed on the lower surface of the electrolytic cell body 32 with respect to the other end of the upper cover 37.
  • the anode piece and the cathode piece of the assembled electrolysis device 3 can be respectively locked to the water tank cover 26 by the two electrode columns 33, so that when the water tank body 24 and When the tank lid 26 is tightly coupled, the electrolysis device 3 can be suspended in the tank 2 in a suspended manner.
  • the water tank 2 and the electrolysis device 3 are in communication with each other.
  • the detecting device (such as the flow detector F) is inserted through the plurality of cover holes 261 of the water tank cover 26 Placed on the tank cover 26.
  • the water tank 2 and the condensing filter 6 provided with the electrolysis device 3 are connected between the duct 22 of the water tank 2 and the air inlet hole 60 of the condensing filter 6. Connect to connect to each other.
  • the condensing filter 6 and the humidifying device 9 communicating with the water tank are connected to each other by the connection between the air outlet 60 of the condensing filter 6 and the second duct 92 of the humidifying device 9.
  • the atomizing/volatile gas mixing tank 4 is connected to the fourth conduit 98 of the humidification device 9.
  • the water tank 2 houses an electrolyzed water W
  • the electrolysis device 3 is disposed in the water tank 2 for electrolyzing the electrolyzed water W to generate a hydrogen-oxygen mixed gas.
  • the hydrogen-oxygen mixed gas generated in the electrode flow path is input to the first hollow portion 20 via the upper perforation of the corresponding pad 36 and the corresponding first flow path 370 of the upper cover 37.
  • the hydrogen-oxygen mixed gas input to the first hollow portion 20 is further output through the conduit 22 of the water tank 2.
  • the hydrogen-oxygen mixed gas output from the conduit 22 of the water tank 2 is passed through the air inlet 60 of the condensing filter 6 into the condensing filter 6 for condensation and filtration.
  • the hydrogen-oxygen mixed gas entering the air inlet 60 of the condensing filter 6 is firstly filtered first through the filter 600 and the filter cover 602. Then, the preliminary filtered hydrogen-oxygen mixed gas is further introduced into the circulation flow path 640 for condensation, and at the same time, the hydrogen-oxygen mixed gas is filtered by the activated carbon fiber and the filter material disposed in the flow path 640a, and the electrolyte is Adsorbed in the circulation channel 640. Next, the filtered hydrogen-oxygen mixed gas is supplied through the outlet hole 62 of the condensing filter 6 to output the filtered hydrogen-oxygen mixed gas.
  • the filtered hydrogen-oxygen mixed gas is supplied to the humidification device 9 through the second conduit 92 connected to the air outlet 62.
  • the filtered hydrogen-oxygen mixed gas received by the second conduit 92 is perforated by a plurality of nanometers of the two outlet tubes 94 to be discharged into the hollow body 90.
  • the plurality of nanoperforations on the surface of the output tube 94 it can be used to refine the hydrogen-oxygen mixed gas input to the humidification device to form a resolvable refinement bubble.
  • the humidification of the filtered hydrogen-oxygen mixed gas through the humidification device allows the electrolyte content in the hydrogen-oxygen mixed gas to be lower, and can be safely used for human use when dissolved in water.
  • the humidified hydrogen-oxygen mixed gas outputted by the humidification device 9 can be inhaled by the user, but not limited thereto.
  • the humidified hydrogen-oxygen mixture output by the humidification device 9 is used.
  • the gas may be further mixed with the atomizing gas generated via the atomizing/volatile gas mixing tank 4 to form a health gas for inhalation by the user.
  • the water pump device is used to extract the gas inside the water tank 2 to generate a negative pressure inside thereof.
  • the supplemental water that has been replenished via the third conduit 96 is input from the humidification device 9 back into the water tank 2 in which the electrolysis device 3 is disposed by the above-described negative pressure. More specifically, the connection between the supplementary water by the second duct 92 of the humidifying device 9 and the air outlet 62 of the condensing filter 6 is input to the condensing filter 6 by the humidifying device 9.
  • the electrolyte adsorbed in the circulation flow path 640 of the condensing filter 6 can be backflushed into the water tank 2 provided with the electrolysis device 3 through the inlet holes 60 and the conduit 22 by the above-mentioned supplementary water to restore the circulation flow path.
  • the gas generator produces a hydrogen-oxygen mixed gas flow rate of 120 liters per hour After 2,000 to 3,000 hours of operation, the loss of electrolyte is less than or equal to 50 grams, but not limited to this. In practical applications, it can also be estimated that when the gas generator generates a hydrogen-oxygen mixed gas flow rate of 600 liters per hour and operates for 40 to 60 hours, the electrolyte loss is less than or equal to 5 grams.
  • the present invention utilizes makeup water to backflush the electrolyte into a water tank 2 provided with an electrolysis device 3, which can be used to provide electrolyzed water required for electrolysis device 3 to perform electrolysis. Further, the electrolyzed water supplementing the first hollow portion 20 of the input water tank 2 is input to the corresponding electrode flow path via the second flow path 380 of the lower cover 38 of the electrolysis device 3 and the plurality of lower perforations of the electrolytic cell body. In order to provide the electrolyzed water W required for electrolysis of the electrolysis device 3.
  • the gas generator of the present invention can detect the water level contained in the first hollow portion of the water tank and/or the electrolysis device by a water level gauge to control the replenishment of the electrolyzed water.
  • the flow detector F can be coupled to the electrolysis device 3 to detect the flow rate of the hydrogen-oxygen mixed gas.
  • the flow rate of the hydrogen-oxygen mixed gas of the gas generator 1 is between 0.01 L/min. and 12 L/min.
  • the electrolyte loss is less than or equal to 50 grams; it can also be estimated as the flow rate of the hydrogen-oxygen mixed gas generated by the gas generator.
  • the loss of electrolyte is less than or equal to 5 grams; it can also be estimated as the flow rate of the hydrogen-oxygen mixed gas generated by the gas generator is 30 liters per hour and operates for 40 to 60 hours.
  • the loss of the electrolyte is less than or equal to 0.25 g; it can also be estimated that when the flow rate of the hydrogen-oxygen mixed gas generated by the gas generator is 240 liters per hour and the operation is 40 to 60 hours, the loss of the electrolyte is less than or equal to 2 g; It can be estimated that when the gas generator generates a hydrogen-oxygen mixed gas flow rate of 360 liters per hour and operates for 40 to 60 hours, the electrolyte loss is less than or equal to 3 grams; or it can be estimated as a gas generator. When the flow rate of the hydrogen-oxygen mixed gas is 3 liters per hour and the operation is performed for 400 to 600 hours, the loss of the electrolyte is 0.25 g or less. However, it is not limited to the above. In actual application, the user can adjust the required flow and operation time according to the demand.
  • FIG. 12 is a schematic view showing another embodiment of the gas generator of the present invention.
  • the gas generator 1 includes a water tank 2, an electrolysis device 3, a condensing filter 6, a humidification filter 8, a humidification device 9, and a water pump device 5.
  • the electrolysis device 3 is disposed inside the water tank 2.
  • the condensing filter 6 is connected between the electrolysis device 3 and the humidification filter 8.
  • the humidification filter 8 houses water and is connected to the condensing filter 6.
  • the humidification device 9 is connected to the humidification filter 8.
  • the condensing filter is used to condense the hydrogen-oxygen mixed gas produced by the electrolysis device and filter the electrolyte in the hydrogen-oxygen mixed gas.
  • the humidification filter is used to filter the hydrogen-oxygen mixed gas filtered by the condensing filter.
  • the humidification device is for humidifying the hydrogen-oxygen mixed gas filtered by the humidification filter.
  • the humidification filter 8 can include a tank, a first conduit, a first filter, and a first conduit.
  • the tank has a space for accommodating water, but it is not limited to the actual application, and the required liquid can be accommodated according to requirements.
  • the first conduit communicates with the exterior and interior of the trough body having a first end and a second end corresponding to the first end, and the first end and the second end are connectable to the exterior and interior of the trough.
  • the first filter member is disposed at the second end of the first conduit.
  • the first pipe communicates with the inside and the outside of the tank.
  • the humidification filter 8 can further include a second filter member located at the outlet or inlet of the first conduit.
  • the second filter element may be disposed under the first pipe, thereby directly outputting the hydrogen-oxygen mixed gas after filtering the water vapor.
  • the first filter element and the second filter element may be made of a porous plastic.
  • the porous plastic may be a polyethylene, but not limited thereto.
  • the first end of the first conduit may receive the hydrogen-oxygen mixed gas from the outside, and then input the hydrogen-oxygen mixed gas into the tank through the second end. Since the first filter member is disposed at the second end, the hydrogen-oxygen mixed gas passes through the first filter member when being outputted from the second end, and the impurities in the hydrogen-oxygen mixed gas are filtered by the first filter member, wherein the impurities may be an electrolyte. After the hydrogen-oxygen mixed gas is supplied to the water contained in the tank, the hydrogen-oxygen mixed gas can be filtered again by the water. After the water-filtered hydrogen-oxygen mixed gas, the water and gas in the hydrogen-oxygen mixed gas may be filtered through the second filter member, and the filtered hydrogen-oxygen mixed gas is output to the outside of the tank through the first pipe.
  • the humidification filter may further comprise a conduit.
  • One end of the branch conduit is in communication with the first end and the second end of the first conduit, and the other end of the branch conduit has a one-way valve.
  • the one-way valve can be used to block the hydrogen-oxygen mixed gas from being output from the branch conduit. Therefore, when the first conduit receives the hydrogen-oxygen mixed gas from the outside, the hydrogen-oxygen mixed gas is blocked by the one-way valve, and only the first end of the first conduit can be The second end is output to the tank.
  • the one-way valve of the humidification filter can also be used to control a water level (not shown) in the tank.
  • the humidification filter can start to pump back the water in the tank by the one-way valve, and the water in the tank that is pumped back through the one-way valve is discharged to the water through the branch conduit and the first conduit. Outside the tank; until the water level of the water in the tank is lower than a predetermined value, the one-way valve no longer sucks the water inside the tank, so that the water level of the water inside the tank can be maintained at a certain height.
  • the water pump device is connected to the water tank for generating a negative pressure in the water tank, so that the supplementary water is pumped back from the humidification device through the humidification filter and the condensing filter to be input to the water tank, and the electrolyte adsorbed in the condensing filter is returned. Rush to the water tank.
  • the flow rate of the hydrogen-oxygen mixed gas generated by the gas generator is 600 liters per hour and the operation is 40 to 60 hours, the loss of the electrolyte is less than 5 grams.
  • the output voltage of the power source is between about 17 volts (V) and 27 volts (V), and the output current of the power source is about 30 amps (A) to 40 amps ( Between A), that is, the electrolysis device produces an outgas volume of between about 1.5 liters and 4.0 liters per minute.
  • the voltage of each group of electrodes (between the positive and negative electrodes) is between about 1.5 volts (V) and 3 volts (V) during use. If there are eight groups, the voltage used is between 12V and 24V.
  • the output voltage of the power source is between about 5 volts (V) and 24 volts (V)
  • the output current of the power source is about 2 amps ( A) to 150 amps (A)
  • the power of the electrolysis device is between 10 watts (ie about 5V*2A) to 3600 watts (ie about 24V*150A)
  • the electrolysis device can generate 0.01 liters to 12 liters per minute. The amount of gas discharged between liters.
  • the hydrogen-oxygen mixed gas generated by the electrolysis device can be condensed and filtered by the condensing filter, and then humidified by the humidifying device to contain the gas.
  • the amount of electrolyte is lower to provide a mixture of hydrogen and oxygen suitable for human inhalation.
  • another A humidification filter is disposed between the condensing filter and the humidification device, which can again filter impurities in the hydrogen-oxygen mixed gas to provide a hydrogen-oxygen mixed gas more suitable for human inhalation.
  • the supplementary water can be supplied from the humidifying device to the return tank by the operation of the water pump device connected to the water tank.
  • the gas generator of the present invention is capable of replenishing water while replenishing the electrolyte to the electrolysis device to restore the filtration capacity of the circulation flow path, prevent clogging and corrosion of the circulation flow path, and reduce electrolyte consumption.

Landscapes

  • Health & Medical Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Veterinary Medicine (AREA)
  • Emergency Medicine (AREA)
  • Biomedical Technology (AREA)
  • Heart & Thoracic Surgery (AREA)
  • Hematology (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Animal Behavior & Ethology (AREA)
  • General Health & Medical Sciences (AREA)
  • Public Health (AREA)
  • Pulmonology (AREA)
  • Anesthesiology (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Thermal Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)

Abstract

一种气体产生器，包含水箱(2)、电解装置(3)、冷凝过滤器(6)、湿化装置(9)以及水泵装置(5)。水箱(2)容置有电解水。电解装置(3)设置于水箱(2)之内以电解水而产生氢氧混合气体。冷凝过滤器(6)用以冷凝电解装置所产生的氢氧混合气体并过滤其中的电解质，以产生过滤后的氢氧混合气体。湿化装置(9)容置补充水并连接于冷凝过滤器(6)，以湿化过滤后的氢氧混合气体。水泵装置(5)连接水箱(2)，用以于水箱(2)内产生负压，藉以将补充水由湿化装置(9)经由冷凝过滤器(6)回抽以输入至水箱(2)，并将吸附于冷凝过滤器(6)内的电解质回冲至水箱(2)，以减少电解质的损耗。

Description

气体产生器 技术领域
本发明有关于一种气体产生器，特别是有关于一种具有过滤、湿化功能并且减低电解质消耗的气体产生器。
背景技术
一直以来，人类对于生命是十分地重视，许多医疗的技术的开发，都是用来对抗疾病，以延续人类的生命。过去的医疗方式大部分都是属于被动，也就是当疾病发生时，再对症进行医疗，比如手术、给药、甚至癌症的化学治疗、放射性治疗、或者慢性病的调养、复健、矫正等。但是近年来，许多医学专家逐渐朝向预防性的医学方法进行研究，比如保健食品的研究，遗传性疾病筛检与提早预防等，更是主动的针对未来性可能的发病进行预防。另外，为了延长人类寿命，许多抗老化、抗氧化的技术逐渐被开发，且广泛地被大众采用，包含涂抹的保养品及抗氧化食物/药物等。
经研究发现：人体因各种原因，(比如疾病，饮食，所处环境或生活习惯)引生的不安定氧(O+)，亦称自由基(有害自由基)，可以与吸入的氢混合成部份的水，而排出体外。间接减少人体自由基的数量，达到酸性体质还原至健康的碱性体质，可以抗氧化、抗老化，进而也达到消除慢性疾病和美容保健效果。甚至有临床实验显示，对于一些久卧病床的病人，因为长期呼吸高浓度氧，造成的肺损伤，可以透过吸入氢气以缓解肺损伤的症状。
然而，经由电解装置电解电解水后所产生的氢氧混合气体通常具有较高的温度且相对干燥，其并不适合人体直接吸入。同时，在电解过程中亦会有电解水与电解质消耗的问题，而需要补充水及电解质的情形发生。以上问题进而常常造成习知电解装置使用上的不便利。
发明内容
因此，本发明的目的在于提供一种气体产生器，用以电解液态水并产生氢氧混合气体，接着冷凝及过滤氢氧混合气体的电解质，再进行湿化并使气体含电解质量更低，以提供适合人体吸入的氢氧混合气体。另外，再透过补充补充水，并将电解质回冲至电解装置，以恢复循环流道的过滤能力、防止循环流道的阻塞和腐蚀以及减低电解质的消耗。
为实现上述目的，本发明公开了一种气体产生器，其特征在于包含：
一水箱，容置有电解水，该电解水包含电解质；
一电解装置，设置于该水箱之内，用以电解该电解水以产生一氢氧混合气体；
一冷凝过滤器，连接于该电解装置，用以冷凝该电解装置所产生的该氢氧混合气体并过滤该氢氧混合气体中的该电解质，以产生过滤后的该氢氧混合气体；
一湿化装置，容置一补充水并连接于该冷凝过滤器，用以湿化过滤后的该氢氧混合气体；以及
一水泵装置，连接该水箱，用于在该水箱内产生一负压，藉以将该补充水由该湿化装置经由该冷凝过滤器回抽以输入至该水箱，并将吸附于该冷凝过滤器内的该电解质回冲至该水箱；
其中当该气体产生器产生该氢氧混合气体的流量为每小时360～600公升并运作40～60小时后，该电解质的损耗小于3～5克。
其中，该电解质为食用级的氢氧化钠。
其中，另包含一雾化/挥发气体混合槽，其中该雾化/挥发气体混合槽包含一出气口，该水箱与该雾化/挥发气体混合槽藉由该水泵装置相互连通，当该水泵装置运作时将该水箱内部的气体抽取出并由雾化/挥发气体混合槽的该出气口排出，以使该水箱内产生该负压。
其中，该雾化/挥发气体混合槽连接该湿化装置以接收湿化后的该氢氧混合气体，该雾化/挥发气体混合槽产生一雾化气体与湿化后的该氢氧混合气体混合，以形成一保健气体供一使用者吸入，而该雾化气体选自于由水蒸汽、雾化药水、挥发精油及其组合所组成的族群中的一种。
其中，该湿化装置另包含至少一输出管，该至少一输出管具有多个穿孔，该氢氧混合气体经由该至少一输出管的该多个穿孔排出，以湿化过滤后的该氢氧混合气体。
其中，该冷凝过滤器包含多个冷凝片，每一冷凝片具有一流道，该冷凝片的该流道与相邻的该冷凝片的该流道相互连通，藉以形成供该氢氧混合气体流通的一循环流道。
其中，该流道为一渐扩式流道与一连通流道所组成，该冷凝片的该渐扩式流道与相邻的该冷凝片的该渐扩式流道藉由该冷凝片的该连通流道以相互连通。
其中，该流道设置有一活性碳纤维以过滤该氢氧混合气体中的该杂质，该杂质为该电解水中的电解质。
其中，该流道另设置有任一由陶瓷、石英石、硅藻土、海泡石或以上材料组合所组成的过滤材料。
其中，该渐扩式流道为一截面渐扩的流道，该渐扩式流道包含一开口，该连通流道具有一流道及两相对应的开口，该连通流道的该两相对应的开口藉由该流 道以相互连通，该冷凝片的该渐扩式流道的该开口与相邻的该冷凝片的该渐扩式流道的该开口藉由该冷凝片的该连通流道的该两相对应的开口以相互连通。
还公开了一种气体产生器，其特征在于包含：
一水箱，容置有一电解水，该电解水包含一电解质；
一电解装置，设置于该水箱之内，用以电解该电解水以产生一氢氧混合气体；
一冷凝过滤器，连接于该电解装置，用以冷凝该电解装置所产生的该氢氧混合气体并过滤该氢氧混合气体中的该电解质，以产生过滤后的该氢氧混合气体；
一湿化过滤器，容置有水并连接于该冷凝过滤器，用以过滤该冷凝过滤器所过滤的该氢氧混合气体；
一湿化装置，容置一补充水并连接于该湿化过滤器，用以湿化经该湿化过滤器过滤后的该氢氧混合气体；以及
一水泵装置，连接该水箱，用以于该水箱内产生一负压，藉以将该补充水由该湿化装置经由该湿化过滤器以及该冷凝过滤器回抽以输入至该水箱，并将吸附于该冷凝过滤器内的该电解质回冲至该水箱；
其中当该气体产生器产生该氢氧混合气体的流量为每小时360～600公升并运作40～60小时后，该电解质的损耗小于3～5克。
综合而言，本发明的重点在于提出一种气体产生器，于本发明的气体产生器中，电解装置所产生的氢氧混合气体能够先藉由冷凝过滤器进行冷凝及过滤其中的电解质，再藉由湿化装置进行湿化并使气体含电解质量更低，以提供适合人体吸入的氢氧混合气体。于另一实施例中，另可包含位于冷凝过滤器以及湿化装置之间的湿化过滤器，其可再次过滤氢氧混合气体中的杂质，以提供更适合人体吸入的氢氧混合气体。此外，藉由本发明的设计能够用以补充补充水，并将电解质回冲至电解装置，用以恢复循环流道的过滤能力、防止循环流道的阻塞和腐蚀以及减低电解质的消耗。
关于本发明的优点，精神与特征，将以实施例并参照所附图式，进行详细说明与讨论。
附图说明
图1A及图1B：绘示本发明的气体产生器于一实施例中的不同视角的示意图。
图2A、图2B及图2C：绘示本发明的气体产生器于一实施例中的不同视角的示意图。
图3A、图3B及图3C：绘示图2A所示实施例中不具有水箱的外壳、水箱的上盖、湿化器的架体及湿化器的外接管的不同视角的示意图。
图4A及图4B：绘示图3A所示实施例中不具有水箱的不同视角的示意图。
图5A及图5B：绘示图2A所示实施例中仅具有冷凝过滤器及水箱盖体的俯视图及沿该俯视图的A-A线剖设的剖面图。
图6A及图6B：绘示本发明的气体产生器于另一实施例中仅具冷凝过滤器及水箱盖体组合时的不同视角的示意图。
图7：绘示图6所示实施例中不具有水箱盖体时的示意图。
图8：绘示图7所示实施例中不具有过滤网时的示意图。
图9：绘示图8所示实施例中不具有过滤网盖时的示意图。
图10A及图10B：绘示本发明的气体产生器的冷凝过滤器于图6A中所示实施例的俯视图及沿该俯视图的B-B线剖设的剖面图。
图11：绘示本发明的气体产生器于另一实施例中的湿化装置的示意图。
图12：绘示本发明的气体产生器于另一实施例的示意图。
具体实施方式
为了让本发明的优点，精神与特征可以更容易且明确地了解，后续将以实施例并参照所附图式进行详述与讨论。值得注意的是，这些实施例仅为本发明代表性的实施例，其中所举例的特定方法，装置，条件，材质等并非用以限定本发明或对应的实施例。
请先参阅图1A至图3C，图1A及图1B系绘示本发明的气体产生器于一具实施例中的不同视角的示意图，图2A、图2B及图2C系绘示本发明的气体产生器于一具实施例中的不同视角的示意图，图3A、图3B及图3C系绘示图2A所示实施例中不具有水箱的外壳、水箱的上盖、湿化器的架体及湿化器的外接管的不同视角的示意图。本发明的气体产生器1包含水箱2、电解装置3(未绘示于图1A及图1B中，其系绘示于图4A及图4B中)、雾化/挥发气体混合槽4、水泵装置5(未绘示于图1A及图1B中，其系绘示于图2B至图4B中)、冷凝过滤器6、冷却装置7以及湿化装置9。
水箱2容置有电解水，其中电解水包含电解质。电解装置3设置于水箱2内，用以电解电解水以产生一氢氧混合气体。冷凝过滤器6与电解装置3连通，用以接收并冷凝电解装置3所产生的氢氧混合气体，再过滤氢氧混合气体中的电解质，以产生过滤后的氢氧混合气体。湿化装置9用以接收并湿化过滤后的氢氧混合气体。湿化装置9容置一补充水并连通水箱2的第一中空部20。水泵装置5连通水箱2的第一中空部20。当水泵装置运作时，水泵装置5抽取水箱2的第一中空部20内部的气体以使水箱2内部产生一负压。湿化装置9藉由负压将补充水回冲至冷凝过滤器6并补充输入至水箱2内，以降低电解质的损耗。其中氢氧混合气体的流量为每小时120公升，当气体产生器运作2,000～3,000小时(hr)，电解质的损耗小于等于50克；亦可以将其预估为当气体产生器产生氢氧混合气体的流量为每小时600公升并运 作40～60小时后，电解质的损耗小于等于5克。而冷却装置7设置于水箱2的盖体上并与水箱相互连通，可用以冷却产生氢氧混合气体后的电解水。以下将对本发明的各个元件的设计先分别进行说明。
请参阅图5A至图6B，图5A及图5B系绘示图2A所示实施例中仅具有冷凝过滤器及水箱盖体的俯视图及沿该俯视图的A-A线剖设的剖面图。图6A及图6B系绘示本发明的气体产生器于另一实施例中仅具冷凝过滤器及水箱盖体组合时的不同视角的示意图。水箱2具有一第一中空部20。水箱2的第一中空部20系适于容纳一电解水。电解水包含一电解质，其为氢氧化钠。惟不以此为限，于实际应用时，电解质得为碳酸钙，氯化钠等，甚至亦可以为食用级的氢氧化纳。水箱2另包含有一导管22、一水箱槽体24及一水箱盖体26。水箱槽体24内部的空间即为第一中空部20。导管22设置于水箱盖体26，藉以连通冷凝过滤器6与水箱2，用以输出由电解装置3所产生的氢氧混合气体以及补充输入电解水至水箱2内。水箱盖体26可包含有多个盖孔，多个盖孔连通水箱2的第一中空部20，用以供电解装置3的电极柱33(如图4A所示)贯穿以将电解装置3设置于水箱上，或者用以供检测装置(如流量侦测器、水位计、安全阀)贯穿并设置于其上。
请参阅图4A及图4B，图4A及图4B系绘示图3A所示实施例中不具有水箱的不同视角的示意图。电解装置3包含一电解槽体32、多个电极(未绘示于图中)、垫板36、上盖体37以及下盖体38。其中多个电极可分别间隔设置于电解槽体32之内并形成多个电极流道。电解槽体的底部可具有多个下穿孔。垫板36设置于每一电极的上表面。垫板可具有多个上穿孔。上盖体37盖设于垫板36相对于电解槽体32的另一端。上盖体37可具有至少一第一流道370。位于垫板36的多个上穿孔与第一中空部20系藉由上盖体37的至少一第一流道370相互连通。下盖体38盖设于电解槽体32的下表面相对于上盖体37的另一端。下盖体38包含至少一第二流道380。位于电解槽体32的底部的多个下穿孔与第一中空部20系藉由下盖体38的至少一第二流道380相互连通。
请参阅图5A至图10B，图7系绘示图6所示实施例中不具有水箱盖体时的示意图。图8系绘示图7所示实施例中不具有过滤网时的示意图。图9系绘示图8所示实施例中不具有过滤网盖时的示意图。图10A及图10B系绘示本发明的气体产生器的冷凝过滤器于图6A中所示实施例的俯视图及沿该俯视图的B-B线剖设的剖面图。冷凝过滤器6具有一入气孔60以及一出气孔62。入气孔60得连通于电解装置3，用以接收氢氧混合气体。出气孔62用以排出过滤后的氢氧混合气体。另外，本发明的冷凝过滤器6包含有多个冷凝片64。每一冷凝片64具有一流道640a，冷凝片64的流道640a与相邻的冷凝片64的流道640a相互连通，藉以形成供氢氧混合气体流通的一循环流道640，用以冷凝氢氧混合气体。入气孔60与出气孔62得藉由循环流道640 相互连通。
于一实施例中，冷凝片64的流道640a为一渐扩式流道642和一连通流道644所组成。如图5B及图10B所示，渐扩式流道642为一截面渐扩的流道，惟不以图5B及图10B所示的渐扩式流道642为限，于实际应用时，渐扩式流道的横截面得呈半圆型、三角型或梯形。渐扩式流道642具有相对宽的一端及相对窄的一端。渐扩式流道642的相对宽的一端及相对窄的一端皆具有一开口。连通流道644具有一流道及两个相对应的开口。连通流道644的两个相对应的开口得藉由流道相互连通。于一实施例中，当渐扩式流道642与连通流道644相互连接时，渐扩式流道642与连通流道644藉由渐扩式流道642的相对宽的一端的开口与连通流道644的开口的连接得以相互连通。冷凝片64的流道640a的结构设计，其使得水平流道(即渐扩式流道642)与垂直流道(即连通流道644)得以相互连通，惟水平流道不以截面渐扩的流道为限，于实际应用时，水平流道亦可以为截面相等的流道。更进一步地，当冷凝片64的流道640a与相邻冷凝片64的流道640a相互连接时，冷凝片64的流道640a与相邻冷凝片64的流道640a藉由冷凝片64的渐扩式流道642的相对窄的一端的开口与相邻冷凝片64的连通流道644的开口的连接得以相互连通。因此，冷凝片64的流道640a的结构设计，其使得冷凝片64的流道640a与相邻冷凝片64的流道640a得以相互连通，藉以形成供氢氧混合气体流通的循环流道640。意即于本实施例中，冷凝片与相邻冷凝片的连接方式，能驱使氢氧混合气体通过较长的冷凝及过滤路径，进而达到更佳的冷凝及过滤效果。更进一步地，于一实施例中，流道640a内得设置有一活性碳纤维，用以过滤氢氧混合气体中的电解质。流道640a得另设置有任一由陶瓷、石英石、硅藻土、海泡石或以上组合所组成的过滤材料，过滤材料能更进一步地过滤氢氧混合气体中的电解质。此外，于一实施例中，本发明的入气孔60得由一过滤网600及一过滤网盖602所组成。过滤网600及过滤网盖602得连通于电解装置3，用以接收氢氧混合气体，并初步地过滤氢氧混合气体。
于一实施例中，如图5B所示，循环流道640可藉由两组流道640a所组成即可达到冷凝的功效，同时能使冷凝过滤器6的设计简化以及成本降低，惟不以此为限，于实际应用时，可以根据设计者的需求调整流道的数量。
请参阅图2C及图11，图11系绘示本发明的气体产生器于另一实施例中的湿化装置的示意图。本发明的湿化装置9包含有一中空本体90、一第二导管92、至少一输出管94、一第三导管96以及一第四导管98。中空本体90得用以容置一补充水。第二导管92设置于中空本体90上得用以与电解装置3连通(未绘示于图中)。至少一输出管94设置于中空本体90的中并与第二导管92连接。第二导管92系与两输出管94连接以形成一T型结构，惟不以此为限，于实际应用时，得视使用情况作调整第二导管与至少一输出管94之间的连接。
更进一步地，两输出管94的表面皆具有多个穿孔。于一实施例中，穿孔得具有奈米级的孔径为介于2奈米至10奈米的范围内，用以对气体进行细化以形成易溶解的细化气泡，惟不以此为限，于实际应用时，穿孔的孔径大小得视使用者需求进行调整。连接第二导管92的两输出管94的末端皆分别设置有一橡胶塞，用以使由第二导管92所接收的氢氧混合气体由两输出管94的多个奈米穿孔(未绘示于图中)排出至中空本体90，惟不以此为限，于实际应用时，连接第二导管92的两输出管94的末端亦可为封闭的设计。
第三导管96得设置于中空本体90上，用以补充输入补充水W2。于实际应用时，第三导管得连通一导孔，由第三导管通过导孔以倒出氢气水或者倒入补充水。第四导管98得设置于中空本体90上，用以输出经过湿化后的氢氧混合气体。
请参阅图3B及图4A。水泵装置5得设置于水箱盖体26上并连通于水箱2的第一中空部20，用以抽取水箱2内部的气体以使其内部产生一负压，藉以将补充水由湿化装置9输入至水箱，并将吸附于冷凝过滤器6内的电解质回冲至水箱2的第一中空部20。
请参阅图3B及图4A。雾化/挥发气体混合槽4可连接湿化装置9以接收湿化后的氢氧混合气体。雾化/挥发气体混合槽可产生雾化气体，其中雾化气体得选自于由水蒸汽、雾化药水、挥发精油及其组合所组成的族群中的一种。雾化/挥发气体混合槽可将其产生的雾化气体与湿化后的氢氧混合气体混合，以形成保健气体供使用者吸入。另外，雾化/挥发气体混合槽4可包含一出气口40，惟出气口的设计并不以图四A所示为限，于实际应用时，出气口亦可以为出气管、出气口等，可根据使用者的需求作调整。雾化/挥发气体混合槽4的出气口40与水泵装置5相互连通。于一实施例中，当电解装置3暂停电解电解水以产生氢氧混合气体时，启动水泵装置进行运作，水泵装置5可将水箱内部的气体抽取出并由雾化/挥发气体混合槽4的出气口40排出，以使水箱内产生负压，藉以将补充水由湿化装置输入至水箱，并将吸附于冷凝过滤器内的电解质回冲至水箱。
以上，在对各个元件的个别设计进行说明后，以下将对一种气体产生器的各元件的组合方式以及其应用进行描述。
于组装完成的电解装置3中，多个电极分别间隔设置于电解槽体32，垫板36设置于每一电极的上表面，上盖体37盖设于垫板36相对于电解槽体32的另一端，下盖体38盖设于电解槽体32的下表面相对于上盖体37的另一端。
于组装完成的水箱2及电解装置3中，组装完后的电解装置3的阳极片及阴极片可分别地藉由两电极柱33锁固于水箱盖体26上，藉以当水箱槽体24与水箱盖体26紧密结合时，电解装置3可悬空地固设于水箱2内。其中，水箱2与电解装置3为相互连通的。而检测装置(如流量侦测器F)被贯穿于水箱盖体26的多个盖孔261并设 置于水箱盖体26上。
于组装完成的水箱2、电解装置3及冷凝过滤器6中，设置有电解装置3的水箱2与冷凝过滤器6系藉由水箱2的导管22及冷凝过滤器6的入气孔60之间的连接以相互连通。接着，与水箱相互连通的冷凝过滤器6与湿化装置9系藉由冷凝过滤器6的出气孔60与湿化装置9的第二导管92之间的连接以相互连通。更进一步地，雾化/挥发气体混合槽4得连接于湿化装置9的第四导管98。
于实际应用时，水箱2容置有一电解水W，电解装置3设置于水箱2内，用以电解该电解水W以产生一氢氧混合气体。产生于电极流道的氢氧混合气体经由所对应的垫板36的上穿孔以及所对应的上盖体37的第一流道370输入至第一中空部20。输入至第一中空部20的氢氧混合气体进一步地经由水箱2的导管22输出。由水箱2的导管22输出的氢氧混合气体得经由冷凝过滤器6的入气孔60进入冷凝过滤器6进行冷凝及过滤。进入冷凝过滤器6的入气孔60的氢氧混合气体首先会先通过过滤网600及过滤网盖602进行初步地过滤。接着，进行初步地过滤后的氢氧混合气体会进一步地进入循环流道640进行冷凝，同时，氢氧混合气体得藉由设置于流道640a内的活性碳纤维及过滤材料进行过滤并将电解质会吸附于循环流道内640内。接着，过滤后的氢氧混合气体得藉由冷凝过滤器6的出气孔62输出过滤后的氢氧混合气体。
再者，过滤后的氢氧混合气体得藉由与出气孔62连接的第二导管92输入至湿化装置9。由第二导管92所接收的过滤后的氢氧混合气体得藉由两输出管94的多个奈米穿孔以排出至中空本体90内。于实际应用时，由于输出管94的表面所具有的多个奈米穿孔，其得用于对输入湿化装置的氢氧混合气体进行细化，以形成易溶解的细化气泡。过滤后的氢氧混合气体经由湿化装置的湿化，可让氢氧混合气体中的电解质含量更低，当其溶至水中可安全地供人使用。最后，由湿化装置9输出的湿化后的氢氧混合气体可得供使用者吸入，惟不以此为限，于实际应用时，由湿化装置9输出的湿化后的氢氧混合气体亦可进一步地与经由雾化/挥发气体混合槽4产生的雾化气体混合，以形成保健气体供使用者吸入。
另外，当电解装置3暂停电解电解水以产生氢氧混合气体时，水泵装置得用以抽取水箱2内部的气体以使其内部产生负压。经由第三导管96补充输入的补充水得藉由上述的负压由湿化装置9输入回设置有电解装置3的水箱2内。更明确地说，补充水藉由湿化装置9的第二导管92与冷凝过滤器6的出气孔62之间的连接得由湿化装置9输入至冷凝过滤器6。进一步地，吸附于冷凝过滤器6的循环流道640内的电解质可以藉由上述的补充水经由入气孔60及导管22回冲至设置有电解装置3的水箱2内，用以恢复循环流道的过滤能力、防止循环流道的阻塞及腐蚀及减低电解质的消耗。于一实施例中，当气体产生器产生氢氧混合气体的流量为每小时120公升 并运作2,000～3,000小时后，电解质的损耗小于等于50克，惟不以此为限。于实际应用时，亦可以将其预估为当气体产生器产生氢氧混合气体的流量为每小时600公升并运作40～60小时后，电解质的损耗小于等于5克。
于实务上，本发明系利用补充水将电解质回冲至设置有电解装置3的水箱2内，其能用以提供电解装置3进行电解所需的电解水。更进一步地，补充输入水箱2的第一中空部20的电解水得经由电解装置3的下盖体38的第二流道380以及电解槽体的多个下穿孔输入至所对应的电极流道，以提供电解装置3电解时所需的电解水W。于一实施例中，本发明气体产生器得藉由水位计侦测容置于水箱的第一中空部及/或电解装置内的水位，以控制电解水的补充与否。
请参阅图4B。流量侦测器F可耦接电解装置3，以侦测氢氧混合气体的流量。于一实施例中，气体产生器1的氢氧混合气体的产生流率系介于0.01L/min.与12L/min.之间。当气体产生器产生氢氧混合气体的流量为每小时120公升并运作2,000～3,000小时后，电解质的损耗小于等于50克；亦可以将其预估为当气体产生器产生氢氧混合气体的流量为每小时600公升并运作40～60小时后，电解质的损耗小于等于5克；亦可以将其预估为当气体产生器产生氢氧混合气体的流量为每小时30公升并运作40～60小时后，电解质的损耗小于等于0.25克；亦可以将其预估为当气体产生器产生氢氧混合气体的流量为每小时240公升并运作40～60小时后，电解质的损耗小于等于2克；亦可以将其预估为当气体产生器产生氢氧混合气体的流量为每小时360公升并运作40～60小时后，电解质的损耗小于等于3克；或亦可以将其预估为当气体产生器产生氢氧混合气体的流量为每小时3公升并运作400～600小时后，电解质的损耗小于等于0.25克。惟不以上述为限，于实际应用时，使用者可以根据需求以调整控制所需流量以及运作时间。
请参阅图12，图12系绘示本发明的气体产生器于另一实施例的示意图。于一实施例中，气体产生器1包含水箱2、电解装置3、冷凝过滤器6、湿化过滤器8、湿化装置9以及水泵装置5。电解装置3设置于水箱2之内。冷凝过滤器6连接于电解装置3与湿化过滤器8之间。湿化过滤器8容置有水并连接冷凝过滤器6。湿化装置9连接湿化过滤器8。冷凝过滤器用以冷凝电解装置所产生的氢氧混合气体并过滤氢氧混合气体中的电解质。湿化过滤器用以过滤冷凝过滤器所过滤的氢氧混合气体。湿化装置用以湿化经湿化过滤器过滤后的氢氧混合气体。
湿化过滤器8可包含有槽体、第一导管、第一过滤件以及第一管道。槽体有一容置空间，可用来容置水，但于实际应用时并不以此为限，而可以根据需求容置所需的液体。第一导管连通槽体的外部与内部，其具有第一端以及对应第一端的第二端，且第一端与第二端可连通槽体外部与内部。第一过滤件设置于第一导管的第二端。第一管道连通槽体内部与外部。
于一实施例中，湿化过滤器8可进一步地包含一第二过滤件，其位于第一管道的出口或入口。于实际应用时，第二过滤件可设置于第一管道下，藉以将过滤水气后的氢氧混合气体直接输出。第一过滤件及第二过滤件可由一多孔性塑料所制成。于一实施例中，多孔性塑料可为一聚乙烯，惟不以此为限。
第一导管的第一端可由外部接收氢氧混合气体，再经由第二端将氢氧混合气体输入至槽体内。由于第一过滤件设置在第二端，氢氧混合气体由第二端输出时会经过第一过滤件，并藉第一过滤件过滤掉氢氧混合气体中的杂质，其中杂质可为电解质。氢氧混合气体输入至槽体内所容置的水后，可藉由水再次过滤氢氧混合气体。经过水过滤后的氢氧混合气体，可再经过第二过滤件过滤掉氢氧混合气体中的水气，并经由第一管道将过滤后的氢氧混合气体输出至槽体外。
于一实施例中，湿化过滤器还可包含一支导管。支导管的一端连通于第一导管的第一端与第二端之间，并且支导管的另一端具有一单向阀。单向阀可用以阻挡氢氧混合气体由支导管输出，因此当第一导管由外部接收氢氧混合气体时，氢氧混合气体会被单向阀所阻挡，仅可由第一导管的第一端往第二端输出至槽体中。于一实施例中，湿化过滤器的单向阀亦可用以控制槽体内的一水位(未绘示)。当水位为超过一预定值时，湿化过滤器可藉由单向阀开始反抽槽体内的水，同时经由单向阀所反抽的槽体内的水会经由支导管及第一导管排出至槽体外；直到槽体内水的水位低于预定值时，单向阀不再抽吸槽体内部的水，使得槽体内部水的水位可维持在一定高度。
水泵装置连接水箱，用以于水箱内产生一负压，藉以将补充水由湿化装置经由湿化过滤器以及冷凝过滤器回抽以输入至水箱，并将吸附于冷凝过滤器内的电解质回冲至水箱。其中当气体产生器产生氢氧混合气体的流量为每小时600公升并运作40～60小时后，该电解质的损耗小于5克。
于一实施例中，当电解装置与外部电源电连接，电源的输出电压约为17伏特(V)至27伏特(V)之间，电源的输出电流约为30安培(A)至40安培(A)之间，即电解装置约产生每分钟1.5公升至4.0公升之间的出气量。于使用时每一组电极(正负极之间)的电压约1.5伏特(V)至3伏特(V)之间，如有八组则使用的电压为12V～24V之间。惟不以此为限，于实际应用时，当电解装置与外部电源电连接，电源的输出电压约为5伏特(V)至24伏特(V)之间，电源的输出电流约为2安培(A)至150安培(A)之间，即电解装置的功率约为10瓦(即约5V*2A)至3600瓦(即约24V*150A)之间，电解装置能产生每分钟0.01公升至12公升之间的出气量。
综上所述，于本发明的气体产生器中，电解装置所产生的氢氧混合气体能够藉由冷凝过滤器进行冷凝及过滤其中的电解质，再藉由湿化装置进行湿化并使气体含电解质量更低，以提供适合人体吸入的氢氧混合气体。于另一实施例中，另 包含位于冷凝过滤器以及湿化装置之间的湿化过滤器，其可再次过滤氢氧混合气体中的杂质，以提供更适合人体吸入的氢氧混合气体。另外，藉由连通于水箱的水泵装置的运作，能将补充水由湿化装置输入补充回水箱。此外，本发明的气体产生器能够在补充水的同时并将电解质回冲至电解装置，用以恢复循环流道的过滤能力、防止循环流道的阻塞和腐蚀以及减低电解质的消耗。
藉由以上较佳具体实施例的详述，系希望能更加清楚描述本发明的特征与精神，而并非以上述所揭露的较佳具体实施例来对本发明的范畴加以限制。相反地，其目的是希望能涵盖各种改变及具相等性的安排于本发明所欲申请的专利范围的范畴内。虽然本发明已以实施方式揭露如上，然其并非用以限定本发明，任何熟习此技艺者，在不脱离本发明的精神和范围内，当可作各种的更动与润饰，因此本发明的保护范围当视后附的申请专利范围所界定者为准。

Claims (11)

  1. 一种气体产生器，其特征在于包含：
    一水箱，容置有电解水，该电解水包含电解质；
    一电解装置，设置于该水箱之内，用以电解该电解水以产生一氢氧混合气体；
    一冷凝过滤器，连接于该电解装置，用以冷凝该电解装置所产生的该氢氧混合气体并过滤该氢氧混合气体中的该电解质，以产生过滤后的该氢氧混合气体；
    一湿化装置，容置一补充水并连接于该冷凝过滤器，用以湿化过滤后的该氢氧混合气体；以及
    一水泵装置，连接该水箱，用于在该水箱内产生一负压，藉以将该补充水由该湿化装置经由该冷凝过滤器回抽以输入至该水箱，并将吸附于该冷凝过滤器内的该电解质回冲至该水箱；
    其中当该气体产生器产生该氢氧混合气体的流量为每小时360～600公升并运作40～60小时后，该电解质的损耗小于3～5克。
  2. 如权利要求1所述的气体产生器，其特征在于，该电解质为食用级的氢氧化钠。
  3. 如权利要求1所述的气体产生器，其特征在于，另包含一雾化/挥发气体混合槽，其中该雾化/挥发气体混合槽包含一出气口，该水箱与该雾化/挥发气体混合槽藉由该水泵装置相互连通，当该水泵装置运作时将该水箱内部的气体抽取出并由雾化/挥发气体混合槽的该出气口排出，以使该水箱内产生该负压。
  4. 如权利要求3所述的气体产生器，其特征在于，该雾化/挥发气体混合槽连接该湿化装置以接收湿化后的该氢氧混合气体，该雾化/挥发气体混合槽产生一雾化气体与湿化后的该氢氧混合气体混合，以形成一保健气体供一使用者吸入，而该雾化气体选自于由水蒸汽、雾化药水、挥发精油及其组合所组成的族群中的一种。
  5. 如权利要求1所述的气体产生器，其特征在于，该湿化装置另包含至少一输出管，该至少一输出管具有多个穿孔，该氢氧混合气体经由该至少一输出管的该多个穿孔排出，以湿化过滤后的该氢氧混合气体。
  6. 如权利要求1所述的气体产生器，其特征在于，该冷凝过滤器包含多个冷凝片，每一冷凝片具有一流道，该冷凝片的该流道与相邻的该冷凝片的该流道相互连通，藉以形成供该氢氧混合气体流通的一循环流道。
  7. 如权利要求6所述的气体产生器，其特征在于，该流道为一渐扩式流道与一连通流道所组成，该冷凝片的该渐扩式流道与相邻的该冷凝片的该渐扩式流道藉由该冷凝片的该连通流道以相互连通。
  8. 如权利要求6所述的气体产生器，其特征在于，该流道设置有一活性碳纤维以过滤该氢氧混合气体中的该杂质，该杂质为该电解水中的电解质。
  9. 如权利要求6所述的气体产生器，其特征在于，该流道另设置有任一由陶瓷、石英石、硅藻土、海泡石或以上材料组合所组成的过滤材料。
  10. 如权利要求7所述的气体产生器，其特征在于，该渐扩式流道为一截面渐扩的流道，该渐扩式流道包含一开口，该连通流道具有一流道及两相对应的开口，该连通流道的该两相对应的开口藉由该流道以相互连通，该冷凝片的该渐扩式流道的该开口与相邻的该冷凝片的该渐扩式流道的该开口藉由该冷凝片的该连通流道的该两相对应的开口以相互连通。
  11. 一种气体产生器，其特征在于包含：
    一水箱，容置有一电解水，该电解水包含一电解质；
    一电解装置，设置于该水箱之内，用以电解该电解水以产生一氢氧混合气体；
    一冷凝过滤器，连接于该电解装置，用以冷凝该电解装置所产生的该氢氧混合气体并过滤该氢氧混合气体中的该电解质，以产生过滤后的该氢氧混合气体；
    一湿化过滤器，容置有水并连接于该冷凝过滤器，用以过滤该冷凝过滤器所过滤的该氢氧混合气体；
    一湿化装置，容置一补充水并连接于该湿化过滤器，用以湿化经该湿化过滤器过滤后的该氢氧混合气体；以及
    一水泵装置，连接该水箱，用以于该水箱内产生一负压，藉以将该补充水由该湿化装置经由该湿化过滤器以及该冷凝过滤器回抽以输入至该水箱，并将吸附于该冷凝过滤器内的该电解质回冲至该水箱；
    其中当该气体产生器产生该氢氧混合气体的流量为每小时360～600公升并运作40～60小时后，该电解质的损耗小于3～5克。
PCT/CN2016/092990 2015-08-11 2016-08-03 气体产生器 WO2017024969A1 (zh)

Priority Applications (8)

Application Number Priority Date Filing Date Title
SG11201801139TA SG11201801139TA (en) 2015-08-11 2016-08-03 Gas generator
ES16834593T ES2923768T3 (es) 2015-08-11 2016-08-03 Generador de gas
MYPI2018700490A MY189853A (en) 2015-08-11 2016-08-03 Gas generator
US15/751,017 US10869988B2 (en) 2015-08-11 2016-08-03 Gas generator
PL16834593.2T PL3336220T3 (pl) 2015-08-11 2016-08-03 Generator gazu
KR1020187006467A KR102097382B1 (ko) 2015-08-11 2016-08-03 가스 발생기
EP16834593.2A EP3336220B1 (en) 2015-08-11 2016-08-03 Gas generator
JP2018506556A JP6665975B2 (ja) 2015-08-11 2016-08-03 ガス発生装置

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN201510488043.3A CN106435633B (zh) 2015-08-11 2015-08-11 气体产生器
CN201510488043.3 2015-08-11

Publications (1)

Publication Number Publication Date
WO2017024969A1 true WO2017024969A1 (zh) 2017-02-16

Family

ID=57983457

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CN2016/092990 WO2017024969A1 (zh) 2015-08-11 2016-08-03 气体产生器

Country Status (10)

Country Link
US (1) US10869988B2 (zh)
EP (1) EP3336220B1 (zh)
JP (1) JP6665975B2 (zh)
KR (1) KR102097382B1 (zh)
CN (1) CN106435633B (zh)
ES (1) ES2923768T3 (zh)
MY (1) MY189853A (zh)
PL (1) PL3336220T3 (zh)
SG (1) SG11201801139TA (zh)
WO (1) WO2017024969A1 (zh)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106968841A (zh) * 2017-04-20 2017-07-21 李长生 一种电解产生氢氧设备
US10869988B2 (en) 2015-08-11 2020-12-22 Hsin-Yung Lin Gas generator
US11186914B2 (en) 2017-08-25 2021-11-30 Hsin-Yung Lin Water electrolysis device
CN115404494A (zh) * 2022-09-21 2022-11-29 广东骏丰频谱股份有限公司 一种电解装置

Families Citing this family (22)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10465300B2 (en) * 2014-10-16 2019-11-05 Hsin-Yung Lin Gas generator
CN108531929B (zh) * 2017-03-03 2021-04-13 林信涌 气体产生器
CN108531930B (zh) * 2017-03-06 2020-02-04 林信涌 气体产生器
WO2018190322A1 (ja) * 2017-04-12 2018-10-18 隆 竹原 電気分解式ガス吸引具
CN108796533B (zh) * 2017-05-04 2020-09-25 林信涌 气体产生器
CN109385642B (zh) * 2017-08-04 2021-04-13 林信涌 气体产生器
CN108624901B (zh) 2017-08-25 2020-09-15 林信涌 电解水装置
CN108330500A (zh) * 2018-02-13 2018-07-27 中山市陶净科技有限公司 高纯度氢气氧气生产系统
CN108584878A (zh) * 2018-07-03 2018-09-28 湖州市道场乡资产经营有限公司 一种家用制氧机
TWI668332B (zh) 2018-12-04 2019-08-11 林信湧 堆疊式產氫裝置
CN109498877A (zh) * 2018-12-27 2019-03-22 陈可 便携式护理仪
WO2020202638A1 (ja) * 2019-04-03 2020-10-08 中村　正一 酸素吸入器
TWI715976B (zh) * 2019-05-07 2021-01-11 大陸商上海潓美醫療科技有限公司 具有氫水杯之整合式氫氣產生器
CN112013705A (zh) * 2019-05-28 2020-12-01 上海潓美医疗科技有限公司 散热器及具有散热功能的氢气产生器
CN112336953A (zh) * 2019-08-06 2021-02-09 林信涌 正压呼吸设备
WO2021099649A1 (es) * 2019-11-20 2021-05-27 Hydris Ecotech, S.L. Dispositivo para generar gas oxhídrico (hho) y sistema para el mismo fin que incluye dicho dispositivo
TWM590590U (zh) * 2019-12-06 2020-02-11 威臣科技股份有限公司 多功能氫氣生成機
CN113621973B (zh) * 2020-05-07 2024-08-09 上海潓美医疗科技有限公司 可选择性地调整气体流向的氢气产生器
US11229922B2 (en) * 2020-06-22 2022-01-25 Bgt Materials Limited Portable hydrogen-containing ozone water humidifier
CN111748823B (zh) * 2020-06-28 2024-06-21 安徽明天氢能科技股份有限公司 一种除湿、恒温氢氧机
WO2022017311A1 (zh) * 2020-07-23 2022-01-27 林信涌 混合气体产生系统
CN115772676B (zh) * 2021-09-08 2024-01-26 林信涌 具有散热器的氢气产生装置

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20100064892A1 (en) * 2006-01-30 2010-03-18 Hy-Drive Technologies Ltd. Gas/liquid separator for hydrogen generating apparatus
CN103785091A (zh) * 2014-01-07 2014-05-14 林信涌 保健气体产生系统
WO2014170337A1 (en) * 2013-04-16 2014-10-23 Clean Power Hydrogen Limited A hydrogen gas generator system
CN205055130U (zh) * 2015-08-05 2016-03-02 林信涌 湿化过滤器及具有湿化过滤器的气体产生装置
CN105498065A (zh) * 2014-10-16 2016-04-20 林信湧 气体产生器
CN105624723A (zh) * 2014-10-16 2016-06-01 林信湧 气体产生器
CN105624724A (zh) * 2014-10-16 2016-06-01 林信湧 气体产生器
CN105617503A (zh) * 2014-10-16 2016-06-01 林信湧 气体产生器

Family Cites Families (31)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5209906A (en) * 1991-05-10 1993-05-11 Her Majesty The Queen In Right Of Canada, As Represented By The Minister Of National Defence Modular isothermal reactor
JP3192728B2 (ja) * 1992-01-31 2001-07-30 マツダ株式会社 自動車のニープロテクター
FR2746656B1 (fr) * 1996-03-26 1999-05-28 System Assistance Medical Nebuliseur a capteur de pression
JPH1055814A (ja) * 1996-08-08 1998-02-24 Fuji Electric Co Ltd 水素貯蔵発電システム
TW450942B (en) 1998-09-21 2001-08-21 Wang Min Shin Hydrogen and oxygen generation device
KR100296495B1 (ko) 1999-03-31 2001-07-03 윤영환 수소산소 혼합가스 발생장치
US6797241B2 (en) * 2000-12-20 2004-09-28 Delphi Technologies, Inc. Non-thermal plasma reactor having individually retained positive and negative reactor plates
KR100500386B1 (ko) * 2003-03-26 2005-07-18 신중달 수소산소 혼합가스발생장치의 냉각시스템
JP2005179709A (ja) 2003-12-17 2005-07-07 Toyo Tanso Kk ガス発生装置
US20060046113A1 (en) * 2004-08-31 2006-03-02 Sarnoff Corporation Stacked reactor with microchannels
KR100684685B1 (ko) * 2005-03-17 2007-02-20 김춘식 수소 및 산소 혼합가스 발생장치
GB0524486D0 (en) 2005-12-01 2006-01-11 Rolls Royce Fuel Cell Systems An electrolysis apparatus
JP4074322B2 (ja) * 2006-07-06 2008-04-09 炳霖 ▲楊▼ 電気分解を利用した燃焼ガス発生装置及び車載用燃焼ガス発生装置
KR100862923B1 (ko) 2008-07-14 2008-10-13 황부성 수소산소 혼합가스 발생시스템
AU2011288191B2 (en) * 2010-08-13 2016-03-17 Fisher & Paykel Healthcare Limited Apparatus and method for providing gases to a user
CN201912599U (zh) * 2011-01-28 2011-08-03 重庆医科大学附属第一医院 氢气治疗仪
KR101109747B1 (ko) * 2011-04-06 2012-02-15 (주)신행건설 분진 및 가스상의 대기오염물질 동시 제거를 위한 활성탄 및 이를 이용한 박판 전극의 제조방법
TW201332656A (zh) * 2012-02-14 2013-08-16 Epoch Energy Technology Corp 保健氫氧氣供應設備
JP6480325B2 (ja) * 2012-03-28 2019-03-06 コーニンクレッカ フィリップス エヌ ヴェＫｏｎｉｎｋｌｉｊｋｅ Ｐｈｉｌｉｐｓ Ｎ．Ｖ． 流体の導管のためのガス殺菌／消毒システム及び方法
US20150211131A1 (en) 2012-09-07 2015-07-30 Gamikon Pty Ltd Electrolysis apparatus
JP6231296B2 (ja) * 2013-05-16 2017-11-15 エア・ウォーター株式会社 ガスの減湿装置および方法
US20140360496A1 (en) * 2013-06-06 2014-12-11 Harvey Reese Personal health device
CN109395224A (zh) * 2013-06-19 2019-03-01 上海潓美医疗科技有限公司 保健气体产生器
CN203291354U (zh) * 2013-06-19 2013-11-20 林信涌 防爆式保健气体产生器
CN103806013A (zh) 2013-06-19 2014-05-21 林信涌 气水循环系统
CN203291353U (zh) * 2013-06-19 2013-11-20 林信涌 保健气体产生器
CN103789788A (zh) 2013-11-28 2014-05-14 林信涌 气体产生器
JP2015113516A (ja) * 2013-12-13 2015-06-22 富士フイルム株式会社 水の電気分解システム
US10465300B2 (en) * 2014-10-16 2019-11-05 Hsin-Yung Lin Gas generator
TWM503226U (zh) 2015-03-09 2015-06-21 Hsin-Yung Lin 氣體產生器
CN106435633B (zh) 2015-08-11 2018-11-16 林信涌 气体产生器

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20100064892A1 (en) * 2006-01-30 2010-03-18 Hy-Drive Technologies Ltd. Gas/liquid separator for hydrogen generating apparatus
WO2014170337A1 (en) * 2013-04-16 2014-10-23 Clean Power Hydrogen Limited A hydrogen gas generator system
CN103785091A (zh) * 2014-01-07 2014-05-14 林信涌 保健气体产生系统
CN105498065A (zh) * 2014-10-16 2016-04-20 林信湧 气体产生器
CN105624723A (zh) * 2014-10-16 2016-06-01 林信湧 气体产生器
CN105624724A (zh) * 2014-10-16 2016-06-01 林信湧 气体产生器
CN105617503A (zh) * 2014-10-16 2016-06-01 林信湧 气体产生器
CN205055130U (zh) * 2015-08-05 2016-03-02 林信涌 湿化过滤器及具有湿化过滤器的气体产生装置

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See also references of EP3336220A4 *

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10869988B2 (en) 2015-08-11 2020-12-22 Hsin-Yung Lin Gas generator
CN106968841A (zh) * 2017-04-20 2017-07-21 李长生 一种电解产生氢氧设备
US11186914B2 (en) 2017-08-25 2021-11-30 Hsin-Yung Lin Water electrolysis device
CN115404494A (zh) * 2022-09-21 2022-11-29 广东骏丰频谱股份有限公司 一种电解装置
CN115404494B (zh) * 2022-09-21 2023-05-30 广东骏丰频谱股份有限公司 一种电解装置

Also Published As

Publication number Publication date
US10869988B2 (en) 2020-12-22
CN106435633B (zh) 2018-11-16
ES2923768T3 (es) 2022-09-30
EP3336220A1 (en) 2018-06-20
US20180228995A1 (en) 2018-08-16
JP2018525525A (ja) 2018-09-06
CN106435633A (zh) 2017-02-22
SG11201801139TA (en) 2018-03-28
KR20180051517A (ko) 2018-05-16
MY189853A (en) 2022-03-14
JP6665975B2 (ja) 2020-03-13
EP3336220B1 (en) 2022-05-11
PL3336220T3 (pl) 2022-12-12
KR102097382B1 (ko) 2020-04-06
EP3336220A4 (en) 2019-04-17

Similar Documents

Publication Publication Date Title
WO2017024969A1 (zh) 气体产生器
US11865265B2 (en) Anti-explosion gas generator for health use
EP3398641B1 (en) Anti-explosion gas generator for health use
JP6976291B2 (ja) ガス発生器
TWI570275B (zh) 氣體產生器
TWM505298U (zh) 保健氣體產生系統
TWI557276B (zh) 氣體產生器
KR102419298B1 (ko) 적층형 수소 발생 장치
KR102285638B1 (ko) 이온-교환 멤브레인 전기분해 장치
TW201615894A (zh) 氣體產生器
WO2017020825A1 (zh) 湿化过滤器及具有湿化过滤器的气体产生装置
TW201706002A (zh) 氣體產生器
CN109082679B (zh) 气体产生器
TWM518089U (zh) 濕化過濾器及具有濕化過濾器之氣體產生裝置

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 16834593

Country of ref document: EP

Kind code of ref document: A1

WWE Wipo information: entry into national phase

Ref document number: 15751017

Country of ref document: US

ENP Entry into the national phase

Ref document number: 2018506556

Country of ref document: JP

Kind code of ref document: A

WWE Wipo information: entry into national phase

Ref document number: 11201801139T

Country of ref document: SG

NENP Non-entry into the national phase

Ref country code: DE

ENP Entry into the national phase

Ref document number: 20187006467

Country of ref document: KR

Kind code of ref document: A

WWE Wipo information: entry into national phase

Ref document number: 2016834593

Country of ref document: EP