CN212404301U

CN212404301U - Oxyhydrogen gas and hydrogen-rich water production system

Info

Publication number: CN212404301U
Application number: CN202020607300.7U
Authority: CN
Inventors: 李红传; 黄尚杰; 谢曙; 张建国; 王佩菊
Original assignee: Zhuzhou Baojiekang Hydrogen Technology Co ltd; Dongguan Baojiekang Hydrogen Technology Co ltd
Current assignee: Zhuzhou Baojiekang Hydrogen Technology Co ltd; Dongguan Baojiekang Hydrogen Technology Co ltd
Priority date: 2020-04-20
Filing date: 2020-04-20
Publication date: 2021-01-26
Anticipated expiration: 2030-04-20

Abstract

The utility model discloses a oxyhydrogen gas and hydrogen-rich water production system, including the hydrogen manufacturing module that can produce hydrogen and oxygen, be connected with the hydrogen flow channel and the oxygen runner that are used for carrying the hydrogen and the oxygen that make respectively on the hydrogen manufacturing module, oxyhydrogen gas and hydrogen-rich water production system still include the drinking water tank, the drinking water tank is connected with the drinking water pipe that is used for carrying the drinking water, and the hydrogen warp of production hydrogen flow channel can communicate respectively to drinking water pipe and oxygen runner in order to produce hydrogen-rich water and oxyhydrogen mist. The device can make oxyhydrogen mist and hydrogen-rich water simultaneously, can satisfy people's hydrogen uptake and the requirement of drinking hydrogen-rich water simultaneously.

Description

Oxyhydrogen gas and hydrogen-rich water production system

Technical Field

The utility model relates to a system drinking water equipment field, in particular to oxyhydrogen gas and hydrogen-rich water production system.

Background

Hydrogen-rich water, also called hydrogen-rich water in Japan, can eliminate malignant oxygen free radicals in human body, prevent various diseases, and promote human health. The hydrogen-rich water has various health-care functions for human body, and also has the functions of preventing and treating various diseases of diabetes, cardiovascular and cerebrovascular diseases, rheumatism, brain tumor and the like, and also has the functions of beautifying, losing weight and resisting aging.

The hydrogen absorption is very active and obvious for the sub-health of people and the rehabilitation of a plurality of diseases, and meanwhile, the hydrogen also has the obvious positive effect on the aspect of medical treatment. When absorbing hydrogen, the mixed gas of hydrogen and oxygen, which is prepared by mixing hydrogen and oxygen, can be directly used as respiratory gas for people to inhale, and has health care and treatment effects on human health.

Therefore, drinking hydrogen-rich water and hydrogen absorption will become a new fashion of healthy life in the future, but the existing equipment can only produce hydrogen-rich water or hydrogen, and cannot simultaneously produce hydrogen-rich water and hydrogen-oxygen mixed gas, so that the use is inconvenient, and the requirements of people on hydrogen absorption and hydrogen-rich water drinking cannot be met simultaneously.

SUMMERY OF THE UTILITY MODEL

Based on this, it is necessary to provide an oxyhydrogen gas and hydrogen-rich water production system that can produce an oxyhydrogen gas mixture and hydrogen-rich water simultaneously.

The utility model provides a oxyhydrogen gas and hydrogen-rich water production system, including the hydrogen manufacturing module that can electrolysis generate hydrogen and oxygen, be connected with the hydrogen flow channel and the oxygen runner that are used for carrying the hydrogen and the oxygen that make respectively on the hydrogen manufacturing module, oxyhydrogen gas and hydrogen-rich water production system still include the drinking water tank, the drinking water tank is connected with the drinking water pipe that is used for carrying water, and hydrogen warp hydrogen flow channel can mix in order to make hydrogen-rich water and oxyhydrogen mist with the oxygen in the water and the oxygen runner in the drinking water pipe respectively.

Preferably, the hydrogen flow channel comprises a first hydrogen flow channel and a second hydrogen flow channel, the first hydrogen flow channel is communicated with the oxygen flow channel to prepare hydrogen-oxygen mixed gas, a humidification bottle and a fire light detection device are arranged at the communication position, the prepared hydrogen-oxygen mixed gas is conveyed to the first hydrogen-oxygen outlet, and the second hydrogen flow channel is communicated with the drinking water pipe.

Preferably, the prepared hydrogen-rich water flows through the gas-liquid mixing device and the instantaneous heating module to the hydrogen-rich water outlet; the hydrogen runner with drinking water pipe's intercommunication department is called to dissolve hydrogen intercommunication, oxyhydrogen gas and hydrogen-rich water production system still include concentration detection device and return line that can survey hydrogen-rich water concentration, and the hydrogen-rich water that concentration is substandard can be through return line backward flow is to dissolving hydrogen intercommunication department.

Preferably, the oxyhydrogen gas and hydrogen-rich water production system still includes sealed water tank and nanometer aeration equipment, sealed water tank is located between gas-liquid mixing device and the instantaneous heating module, nanometer aeration equipment be located gas-liquid mixing device with between the sealed water tank.

Preferably, oxyhydrogen gas and hydrogen-rich water production system still includes sealed water tank and nanometer aeration equipment, sealed water tank is located between gas-liquid mixing device and the instantaneous heating module, nanometer aeration equipment is located in the sealed water tank.

Preferably, the oxyhydrogen gas and hydrogen-rich water production system further includes a return line through which excess hydrogen gas is mixed with oxygen gas in the oxygen flow channel and output from the second hydrogen gas outlet, the return line being located on the hydrogen flow channel or on the sealed water tank.

Preferably, the second oxyhydrogen outlet is also provided with a humidification bottle and a fire light detection device.

Preferably, the oxyhydrogen gas and hydrogen-rich water production system further comprises a water supply tank for replenishing water to the hydrogen production module, the water supply tank is communicated with the hydrogen production module through a water supply pipeline, a water supply pump or a one-way valve is arranged on the water supply pipeline,

preferably, a filtering device, an instant heating module and a water quality detection device are further arranged on the water supply pipeline or in the water supply tank, a liquid level detection device is further arranged in the water supply tank, a gas-liquid separation device is further arranged on the hydrogen flow channel, and the gas-liquid separation device conveys separated water to the water supply tank.

Preferably, oxyhydrogen gas and hydrogen-rich water production system still include intelligent control terminal, intelligent control terminal includes intelligent AI chip and thing networked control module, intelligent AI chip with thing networked control module connects, hydrogen manufacturing module with thing networked control module is connected.

Compared with the prior art, the utility model discloses following beneficial effect has:

the utility model provides a hydrogen-oxygen gas and hydrogen-rich water production system can generate hydrogen-rich water and oxyhydrogen mist simultaneously, and hydrogen-rich water can supply the people to drink, and the oxyhydrogen mist can supply the people to inhale, reaches treatment or health care effect. The humidifying bottle can play the cooling to the oxyhydrogen mist, effect such as buffering and regulation humidity, and gas-liquid mixing device can improve the dissolved quantity of hydrogen, improves hydrogen-rich water's concentration, and hydrogen-rich water's concentration can be guaranteed to the return line that sets up, and the return line has improved the utilization ratio of hydrogen for make hydrogen-rich water unnecessary hydrogen make the oxyhydrogen mist with the oxygen mixture again.

Drawings

The foregoing and other objects, features and advantages of the invention will be apparent from the following more particular description of preferred embodiments of the invention, as illustrated in the accompanying drawings. Like reference numerals refer to like parts throughout the drawings, and the drawings are not intended to be drawn to scale in actual dimensions, emphasis instead being placed upon illustrating the principles of the invention.

FIG. 1 is a schematic view of an overall oxyhydrogen gas and hydrogen-rich water production system according to a preferred embodiment of the present invention;

FIG. 2 is a schematic view of an overall oxyhydrogen gas and hydrogen-rich water production system according to another preferred embodiment of the present invention;

FIG. 3 is a schematic structural view of an electrolytic cell of the present invention;

FIG. 4 is an overall view of the electrolytic cell of the present invention.

Detailed Description

In order to facilitate understanding of the present invention, the present invention will be described more fully hereinafter with reference to the accompanying drawings.

It will be understood that when an element is referred to as being "connected" to another element, it can be directly connected to the other element and be integral therewith, or intervening elements may also be present. The terms "mounted," "one end," "the other end," and the like are used herein for illustrative purposes only.

Unless defined otherwise, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this invention belongs. The terminology used in the description herein is for the purpose of describing particular embodiments only and is not intended to be limiting of the invention. As used herein, the term "and/or" includes any and all combinations of one or more of the associated listed items.

Referring to fig. 1-4, the utility model provides a oxyhydrogen gas and hydrogen-rich water production system can generate hydrogen-rich water and oxyhydrogen mist simultaneously, and hydrogen-rich water can supply the people to drink or the bathing etc. and the oxyhydrogen mist can supply the people to breathe, has the efficiency of health care and treatment. The hydrogen-oxygen gas and hydrogen-rich water production system comprises a hydrogen production module 1-1 capable of generating hydrogen and oxygen through electrolysis, wherein the hydrogen production module 1-1 adopts an electrolysis method to produce hydrogen, and the hydrogen and oxygen can be produced through water electrolysis, so the hydrogen production module 1-1 comprises a plurality of electrolytic cells 10, and a hydrogen flow channel 1-11 and an oxygen flow channel 1-12 which are respectively used for conveying the produced hydrogen and oxygen are connected to the hydrogen production module 1-1. The system for producing the oxyhydrogen gas and the hydrogen-rich water further comprises a drinking water tank 2-1, wherein the drinking water tank 2-1 is connected with a drinking water pipe 2-11 for conveying water, and the water can be used for drinking and bathing. The hydrogen generated by the hydrogen production module 1-1 can be respectively mixed with the water in the drinking water pipe 2-11 and the oxygen in the oxygen flow passage 1-12 through the hydrogen flow passage 1-11 to prepare hydrogen-rich water and hydrogen-oxygen mixed gas, namely the hydrogen flow passage 1-11 is communicated with the drinking water pipe 2-11 and the oxygen flow passage 1-12, so that the hydrogen can be mixed with the water in the drinking water pipe 2-11 and the oxygen in the oxygen flow passage 1-12 through the hydrogen flow passage 1-11 to respectively prepare hydrogen-oxygen mixed gas and hydrogen-rich water.

In the preferred embodiment, the hydrogen flow channels 1-11 comprise a first hydrogen flow channel 1-111 and a second hydrogen flow channel 1-112, the first hydrogen flow channel 1-111 is communicated with the oxygen flow channel 1-12 to produce hydrogen and oxygen mixed gas, a humidification bottle 5-13 and a fire light detection device 5-14 are arranged at the communication position, the produced hydrogen and oxygen mixed gas is conveyed to a first hydrogen and oxygen outlet 5-15, and the second hydrogen flow channel 1-112 is communicated with the drinking water pipe 2-11. The humidifying bottle 5-13 arranged at the communication part of the first hydrogen flow channel 1-111 and the oxygen flow channel 1-12 can play a role of cooling the mixed hydrogen and oxygen gas, and can buffer the pressure of the mixed hydrogen and oxygen gas, if the pressure of the mixed hydrogen and oxygen gas is high, the mixed hydrogen and oxygen gas can impact the nose of a patient, so that the patient feels uncomfortable. Because the mixed gas of hydrogen and oxygen that electrolytic cell 10 made contains more vapor, so the effect of humidifying bottle cooling is simultaneously, vapor can cool down the condensation water, so the humidifying bottle can also play the effect of dehumidification, it is different with the humidifying bottle in hospital mainly to be used for the humidification, if the mixed gas of hydrogen and oxygen enters humidifying bottle 5-13 again after other dewatering device at first, the mixed gas of hydrogen and oxygen is too dry, humidifying bottle 5-13 also can play the effect of humidification equally, so humidifying bottle 5-13 can make the mixed gas of hydrogen and oxygen in certain humidity range. In addition, the humidifying bottle 5-13 is generally liquid, water or other liquid which does not harm human bodies, so that the humidifying bottle 5-13 can also enable people to directly observe the flow of the oxyhydrogen mixed gas through bubbles, and the flow of the oxyhydrogen mixed gas can be adjusted by adjusting the corresponding gas valve.

The fire light detection device 5-14 can be positioned at any position between the hydrogen and oxygen mixing position and the first hydrogen and oxygen outlet 5-15, and can be positioned at the upstream or the downstream of the hydrogen humidifying bottle 5-13. The fire light detection devices 5-14 can detect fire light, when the fire is detected, signals can be transmitted to corresponding control circuits, the control circuits immediately turn off the power supply, and the electrolytic cell 10 stops producing hydrogen to prevent explosion.

In addition, a filtering device 5-3 and a gas-liquid separating device 5-11 are arranged on the hydrogen flow channel 1-11, the gas-liquid separating device 5-11 can be positioned at the hydrogen outlet of the hydrogen production module 1-1, so that the hydrogen firstly removes water and then enters a humidifying bottle 5-13, the gas-liquid separating device 5-11 can be a gas-water separator or a water tank or a water bottle capable of performing gas-liquid separation, and the separated water can be conveyed to the water supply tank 3-1 for recycling.

In a preferred embodiment, the oxyhydrogen gas and hydrogen-rich water production system further comprises a concentration detection device 5-4 and a return pipeline 4-1, wherein the concentration detection device can be used for detecting the concentration of hydrogen-rich water, the communication part of the hydrogen flow channel 1-11 and the drinking water pipe 2-11 is called a hydrogen dissolving communication 2-12, and the hydrogen dissolving communication 2-12 can be a common three-way valve, a three-way electromagnetic valve or an ejector and the like, so that better mixing of hydrogen and drinking water can be realized. The hydrogen-rich water with unqualified concentration can flow back to the hydrogen dissolving communication position through the return line 4-1. The hydrogen-rich water system comprises a gas-liquid mixing device 5-1 and an instant heating module 5-2, and hydrogen-rich water flows to a hydrogen-rich water outlet 2-13 through the gas-liquid mixing device 5-1 and the instant heating module 5-2. The gas-liquid mixing device 5-1 can pump the hydrogen-rich water mixed after the hydrogen dissolving communication 2-12 to the hydrogen-rich water outlet 2-13, the gas-liquid mixing device 5-1 can adopt a gas-liquid mixing pump to carry out secondary mixing on the hydrogen-rich water, the concentration of the hydrogen-rich water is further improved, water is sprayed out when the drinking faucet is opened due to the pressure of the hydrogen-rich water belt which is discharged out through the gas-liquid mixing device 5-1, and a pressure release valve 5-8 can be arranged at the outlet of the gas-liquid mixing device 5-1 and used for decompressing the hydrogen-rich water. The instantaneous heating module 5-2 can conveniently prepare hydrogen-rich water with different temperatures, such as water with the temperature of 40-50 ℃ and water with the temperature of 80-100 ℃.

The oxyhydrogen gas and hydrogen-rich water production system also comprises a concentration detection device 5-4 capable of determining the concentration of hydrogen-rich water and a return pipeline 4-1, wherein the return pipeline 4-1 is communicated to the communication position of the second hydrogen flow channel 1-112 and the drinking water pipe 2-11, namely the position 2-12 of dissolved hydrogen communication. When the detecting device detects that the hydrogen-rich water concentration is lower than the set value (different concentration buttons arranged on the machine can preset corresponding set values such as 1500ppb, 2000ppb, 2500ppb and 3000ppb), the hydrogen-rich water can be sent to the hydrogen dissolving communication 2-12 through the return pipeline 4-1 to be mixed for two times or more times, a three-way electromagnetic valve can be arranged on the pipeline, the hydrogen-rich water flows out from the outlet for drinking when the concentration reaches the standard, and if the concentration is not enough, the hydrogen is refluxed and re-dissolved from the return pipeline 4-1, so that the automatic control can be realized until the concentration reaches the set value. Of course, a circulating water pump 5-9 can be arranged on the return pipeline 4-1 to pump the hydrogen-rich water with the concentration lower than the set value to the dissolved hydrogen communication 2-12, and when the concentration meets the requirement, the circulating water pump 5-9 is not started.

In another preferred embodiment, the oxyhydrogen gas and hydrogen-rich water production system further includes a sealed water tank 6-2 between the gas-liquid mixing device 5-10 and the instantaneous heating module 5-2, and a nano-aeration device 6-1 between the gas-liquid mixing device 5-10 and the sealed water tank 6-2. The sealed water tank 6-2 has certain pressure, so that the hydrogen-rich water in the hydrogen-rich water pipeline 4-2 can have certain pressure, and the transportation and drinking are convenient. In addition, the sealed water tank 6-2 also enables better mixing of hydrogen with drinking water. The gas-liquid mixing device can adopt a gas-liquid mixing pump, the gas-liquid mixing pump and the nano aeration device 6-1 can both enable hydrogen to be better mixed with drinking water, the nano aeration device 6-1 can be a porous aeration device, such as foam metal, porous membrane, porous ceramic and the like, so that macromolecular hydrogen in hydrogen-rich water is changed into micro-nano-level micromolecular hydrogen, the dissolving amount of the hydrogen in the water can be increased, and the concentration of the hydrogen-rich water is increased. Another embodiment is that the nano aeration device 6-1 is arranged in the sealed water tank 6-2, the filtered water is directly conveyed to the sealed water tank 6-2, the hydrogen flow passage 1-11 is directly connected to the aeration device 6-1, and the aeration is carried out in the sealed water tank 6-2. Such aeration effect will be a little better.

In a preferred embodiment, the oxyhydrogen gas and hydrogen-rich water production system further includes a return gas line 5-17, and excess hydrogen gas is mixed with oxygen gas in the oxygen gas flow path through the return gas line 5-17 and is output from a second hydrogen gas outlet 5-16, and the return gas line 5-17 is located on the hydrogen gas flow path 1-11 or on the sealed water tank 6-2. Namely, the redundant hydrogen for preparing the hydrogen-rich water can be mixed with the oxygen in the oxygen flow channels 1-12 through the gas return pipelines 5-17, so that the utilization rate of the hydrogen is improved, and the redundant hydrogen for preparing the hydrogen-rich water is mixed with the oxygen to prepare the hydrogen-oxygen mixed gas. The hydrogen is partially dissolved in the drinking water and partially arranged at the upper part of the sealed water tank 6-2, and the gas return pipeline 5-17 can be arranged on the sealed water tank 6-2, so that the hydrogen is directly mixed with the oxygen through the gas return pipeline 5-17. Another embodiment is that the gas return line 5-17 is located in front of the hydrogen dissolving communication 2-12, and because the dissolving amount of hydrogen in water is relatively small, part of hydrogen is mixed with oxygen through the gas return line 5-17 before the hydrogen is mixed with drinking water, so that the utilization rate of hydrogen can be improved.

In a preferred embodiment, the oxyhydrogen gas and hydrogen-rich water production system further comprises a water supply tank 3-1, the water supply tank 3-1 is communicated with the hydrogen production module 1-1 through a water supply pipeline 3-2, the water supply tank 3-1 is used for supplying electrolyzed water to the hydrogen production module 1-1, in addition, the hydrogen production module 1-1 also generates oxygen, and the gas flow passage further comprises an oxygen flow passage 1-12, and the oxygen can flow back to the water supply tank 3-1 through the oxygen flow passage 1-12. The electrolytic cell 10 has a requirement for a water source, which may be pure water or deionized or redistilled water. The water supply tank 3-1 is also internally provided with a water quality detection device 5-5 and a liquid level detection device 5-6. The water quality detection device 5-5 is used for detecting the water quality in the water supply tank 3-1, if the water quality of the water added by a user does not reach the standard, the water quality detection device 5-5 can transmit a signal to a corresponding control circuit, the machine is not started, and the alarm requires the replacement of a water source. The liquid level detection device 5-6 can measure the water level in the water supply tank 3-1, and the liquid level detection device 5-6 can also be connected with a corresponding control circuit to control a corresponding water replenishing pump to replenish water for the water supply tank 3-1, and certainly can also manually replenish water by arranging a water filling port. The tank 3-1 is normally maintained at a water level above 2/3.

The water supply pipeline 3-2 is provided with a filtering device 5-3 and an instant heating module 5-2, and the water supply pipeline 3-2 is also provided with a water supply pump 5-7 or a one-way valve 5-10. The water feeding pump 5-7 is used for supplementing water to the electrolytic cell, and the water feeding pump 5-7 can be automatically controlled by the control circuit to supply water to the electrolytic cell. As the cell 10 operates, less and less water is present in the tank, which in the event of a water shortage will result in the cell burning. Therefore, when the water in the water storage tank 2-1 is lower than a certain set value, such as 1/10 of the whole water tank, the liquid level detection device 5-6 inputs a signal into the control circuit, the machine stops working and gives an alarm (a flash lamp is arranged and flashes), a user is reminded to add water, and the user can check whether the corresponding water feeding pump 5-7 is in failure or whether the water feeding tank 3-1 is in water shortage and the like. In addition, the water feeding pumps 5 to 7 also play a role in pressurization, which is beneficial to increasing the circulation of water in the electrolytic cell 10 and playing a role in reducing the temperature in the electrolytic cell 10. Of course, if the vertical distance between the outlet of the water supply tank 3-1 and the water inlet of the electrolytic cell 10 is large enough to have a certain potential, the water pump 5-7 may not be added when the water in the water supply tank 3-1 can flow into the electrolytic cell with a certain pressure. If the water feeding pump 5-7 is arranged, the water feeding pump 5-7 can be set with interval starting time, the water feeding pump 5-7 is started when the machine starts to be started, and the water in the water feeding tank 3-1 is started again when the water reaches a certain temperature, such as 40 ℃, or the water is started once in half an hour. If the water feeding pump 5-7 is provided, the check valve 5-10 is not provided, and the check valve 5-10 is used for preventing oxygen in the electrolytic cell 10 from flowing back to the water inlet of the electrolytic cell 10, thereby being not beneficial to the inflow of water. If the water supply pump 5-7 is not arranged, the check valve 5-10 can be arranged or the check valve 5-10 can be omitted according to the vertical distance between the outlet of the water supply tank 3-1 and the water inlet of the electrolytic cell 10, because the oxygen in the electrolytic cell 10 does not flow out from the oxygen port but enters the water inlet of the electrolytic cell 10 from the inside of the electrolytic cell 10 when the electrolytic cell 10 starts to start, but the phenomenon that the oxygen enters the water inlet of the electrolytic cell 10 after the electrolytic cell 10 works for a few minutes basically disappears, and the electrolytic cell 10 works normally. Therefore, the feed pump 5-7 and the check valve 5-10 may be provided separately or neither depending on the design of the machine system.

The filtering means 5-3 may filter impurities in the water introduced into the electrolytic cell 10, and the filtering means 5-3 may employ ion exchange resin or the like. The temperature probe can be arranged in the water supply tank 3-1 or on the water supply pipeline 3-2 and is used for detecting the temperature of a water source, because the low temperature or the high temperature is unfavorable for the working efficiency and the service life of the electrolytic cell 10, when the water temperature is low or even freezes, the temperature probe transmits a low-temperature signal to a corresponding control circuit, the machine is not started, the instant heating module 5-2 is immediately started at the moment, ice is melted until the water temperature reaches about 20 ℃, the machine is started to work, and the instant heating module 5-2 stops heating at the moment.

In addition, an electromagnetic valve and a drain pipeline can be arranged between the outlet of the water supply tank 3-1 and the filtering device 5-3, so as to protect the electrolytic cell 10 from being polluted by unqualified water sources. The purpose of the solenoid valve is to protect the electrolytic cell 10 from contamination by the rejected water source, because the rejected water flows into the electrolytic cell 10 even though the machine is not being started up when the user adds the rejected water to the water supply tank 3-1. When the water quality detection device 5-5 detects that the added water is unqualified (such as tap water), the electromagnetic valve is closed to prevent the unqualified water from flowing into the electrolytic cell 10, the machine alarms to require water source replacement, and in order to ensure that the unqualified water in the water supply tank 3-1 can be completely removed, a water discharge pipeline is also arranged between the outlet of the water supply tank 3-1 and the filter device 5-3 and is used for completely removing the unqualified water in the water supply tank 3-1 and preventing the electrolytic cell 10 from being polluted. In order to prevent the hydrogen gas from coming out of the electrolytic cell 10 from carrying a small amount of metallic impurities, a filtering device 5-3 may also be provided at the hydrogen gas outlet.

In addition oxyhydrogen gas and hydrogen-rich water production system still includes intelligent control terminal, intelligent control terminal includes intelligent AI chip and thing networked control module, intelligent AI chip with thing networked control module connects, hydrogen manufacturing module with thing networked control module is connected. The intelligent AI chip may enable a human-to-machine conversation, such as a user may query the machine for: how much the cell 10 is at temperature? How many hours are the cell 10 operated? How long is the cell 10 still in service? How much water is left in the water supply tank 3-1? How does the water quality in the water supply tank 3-1? How much hydrogen rich water (hydrogen rich water) is concentrated? The machine can automatically voice-broadcast the answers. The thing networking control module combines together with APP, can look over the condition of machine on APP, like 10 temperature of electrolytic cell, 10 operating time of electrolytic cell, supply tank 3-1 in have how much water, the quality of water in the supply tank 3-1, hydrogen-rich water (hydrogen-rich water) concentration isoparametric.

The electrolytic cell 10 comprises an end plate 101, an electrode 102, a bipolar plate 103, a gas diffusion layer 105 and a proton exchange membrane 106 which are arranged in sequence from outside to inside, wherein the end plate 101, the electrode 102, the bipolar plate 103 and the gas diffusion layer 105 are all arranged outside the proton exchange membrane (the direction close to the surface layer is the outside). Further, a seal ring 104 is disposed between the bipolar plate 103 and the gas diffusion layer 105. The heat exchange system comprises a heat exchange device body 20, a phase change cavity is arranged in the heat exchange device body 20, the temperature adjusting device and the phase change cavity can directly conduct heat mutually, namely, the temperature adjusting device and a shell of the phase change cavity can be in contact with each other, for example, one surface is in contact with or shares one surface, so that direct heat conduction is realized. The phase change cavity is internally provided with a phase change material which can change phase when being heated or cooled, and the phase change material can absorb or release heat when changing phase, so that high-efficiency heat conduction is realized. On the other hand, when the phase change cavity is heated or cooled, the phase change material is subjected to phase change, the phase change cavity can heat or cool the condensation end 1, and reverse heat conduction is realized.

The electrolytic cell comprises a proton exchange layer 106, wherein a diffusion layer 105, a bipolar plate 103 and an electrode 102 are arranged on two sides of the proton exchange layer 106, and the diffusion layer 105, the bipolar plate 103 and the electrode 102 are sequentially arranged from inside to outside. The electrolytic cell also comprises

gas flow channels

107 and 108 and end plates 101, wherein the end plates 101 are positioned on the outermost sides, first ends of the

gas flow channels

107 and 108 are positioned inside the two end plates 101, second ends of the

gas flow channels

107 and 108 lead out gas by connecting pipe joints outside the end plates 101, and the

gas flow channels

107 and 108 positioned between the two end plates 101 are at least partially arranged in a bent (special-shaped) manner. The pressure of the gas pipe can be increased, the user can feel the gas obviously, and the temperature of the electrolysis module can be reduced.

If the bipolar plate 103 is a metal plate, a hydrophilic layer is added close to the anode end, so that the bipolar plate has a hydrophilic or super-hydrophilic function, plays a role in absorbing water and reduces the outflow of water; the cathode end is close to and is made the hydrophobic layer, has hydrophobic or super hydrophobic effect, can play the moisture content outflow of accelerating on the one hand, and the second aspect is to play the corrosion protection effect, and the third aspect, water is attached to the cathode end, can increase resistance, is unfavorable for electrically conductive and heat transfer, can influence efficiency and life-span.

The diffusion layer 105 is provided with a hydrophilic layer close to the anode end, has a hydrophilic or super-hydrophilic effect and plays a role in water absorption; the cathode end is close to and is made the hydrophobic layer, has hydrophobic or super hydrophobic effect, can play the moisture content outflow of accelerating on the one hand, and the second aspect is to play the corrosion protection effect, and the third aspect, water is attached to the cathode end, can increase resistance, is unfavorable for electrically conductive and heat transfer, can influence efficiency and life-span.

The proton exchange membrane is provided with a hydrophilic layer close to the anode end, has the hydrophilic or super-hydrophilic function and plays a role in water absorption; the cathode end is close to and is made the hydrophobic layer, has hydrophobic or super hydrophobic effect, can play the moisture content outflow of accelerating on the one hand, and the second aspect is to play the corrosion protection effect, and the third aspect, water is attached to the cathode end, can increase resistance, is unfavorable for electrically conductive and heat transfer, can influence efficiency and life-span.

The working process of the system is as follows: the water supply tank provides electrolyzed water for the hydrogen production module through the water supply pipeline, when qualified water enters the electrolytic cell, the power supply and the control system are started, the electrolytic cell electrolyzes the water into hydrogen and oxygen, one path of hydrogen is mixed with drinking water in the drinking water pipe to prepare hydrogen-rich water for drinking or using, and the other path of hydrogen is mixed with the prepared oxygen to form hydrogen-oxygen mixed gas. And redundant hydrogen for preparing hydrogen-rich water is mixed with oxygen through the gas return pipeline to form hydrogen-oxygen mixed gas, and the hydrogen-oxygen mixed gas is supplied to a person for breathing through the other hydrogen-oxygen mixed gas outlet. If hydrogen-rich water concentration reaches the setting value, then hydrogen-rich water flows through hydrogen-rich water export through gas-liquid mixing device, relief valve, instantaneous heating module etc. and is drunk or use by the user, if hydrogen-rich water concentration does not reach the setting value, then takes out again to dissolving hydrogen intercommunication department through circulating water pump, carries out the secondary or mixes many times until concentration reaches the setting value. During the electrolysis process, the water level in the electrolytic cell can be reduced, and the water supply tank can supply water to the electrolytic cell through the water supply pipeline. In the working process of the whole system, the intelligent control terminal can monitor the working process of the whole system through the concentration detection device, the temperature detection device, the liquid level detection device and the like, and the real-time control of the system is realized through the corresponding control circuit.

The technical features of the above embodiments can be arbitrarily combined, and for the sake of brevity, all possible combinations of the technical features in the above embodiments are not described, but should be considered as the scope of the present specification as long as there is no contradiction between the combinations of the technical features.

The above embodiments only express the specific embodiments of the utility model, and the description thereof is more specific and detailed, but not so as to limit the scope of the patent of the utility model. It should be noted that, for those skilled in the art, without departing from the spirit of the present invention, several variations and modifications can be made, which are within the scope of the present invention. Therefore, the protection scope of the present invention should be subject to the appended claims.

Claims

1. The utility model provides a oxyhydrogen gas and hydrogen-rich water production system, its characterized in that, including the hydrogen manufacturing module that can electrolysis generation hydrogen and oxygen, be connected with the hydrogen runner and the oxygen runner that are used for carrying the hydrogen and the oxygen that make respectively on the hydrogen manufacturing module, oxyhydrogen gas and hydrogen-rich water production system still include the drinking water tank, the drinking water tank is connected with the drinking water pipe that is used for carrying water, and hydrogen warp hydrogen runner can mix in order to make hydrogen-rich water and oxyhydrogen mist with the oxygen in the water and the oxygen runner in the drinking water pipe respectively.

2. The oxyhydrogen gas and hydrogen-rich water production system according to claim 1, wherein the hydrogen flow channel comprises a first hydrogen flow channel and a second hydrogen flow channel, the first hydrogen flow channel is connected to the oxygen flow channel to produce an oxyhydrogen mixture gas, a humidification bottle and a flame detector are disposed at the connection, the produced oxyhydrogen mixture gas is delivered to the first hydrogen outlet, and the second hydrogen flow channel is connected to the drinking water pipe.

3. The oxyhydrogen gas and hydrogen-rich water production system according to claim 1, wherein the produced hydrogen-rich water flows through the gas-liquid mixing device and the instantaneous heating module to the hydrogen-rich water outlet; the hydrogen runner with drinking water pipe's intercommunication department is called to dissolve hydrogen intercommunication, oxyhydrogen gas and hydrogen-rich water production system still include concentration detection device and return line that can survey hydrogen-rich water concentration, and the hydrogen-rich water that concentration is substandard can be through return line backward flow is to dissolving hydrogen intercommunication department.

4. The oxyhydrogen gas and hydrogen-rich water production system according to claim 3, further comprising a seal water tank between the gas-liquid mixing device and the instantaneous heating module and a nano-aeration device between the gas-liquid mixing device and the seal water tank.

5. The oxyhydrogen gas and hydrogen-rich water production system according to claim 3, further comprising a sealed water tank located between the gas-liquid mixing device and the instantaneous heating module, and a nano-aeration device located within the sealed water tank.

6. The oxyhydrogen gas and hydrogen-rich water production system according to claim 4, further comprising a return gas line through which excess hydrogen gas is mixed with oxygen gas in the oxygen gas flow path and output from a second hydrogen gas outlet, the return gas line being located on the hydrogen gas flow path or on the sealed water tank.

7. The oxyhydrogen gas and hydrogen-rich water production system according to claim 6, wherein the second oxyhydrogen outlet is also provided with a humidification bottle and a flame detection device.

8. The oxyhydrogen gas and hydrogen-rich water production system according to claim 1, further comprising a water feed tank for replenishing water to the hydrogen production module, the water feed tank communicating with the hydrogen production module through a water feed line, the water feed line having a water feed pump or a check valve disposed thereon.

9. The oxyhydrogen gas and hydrogen-rich water production system according to claim 8, wherein a filtration device, an instantaneous heating module and a water quality detection device are further provided on the water supply line or in the water supply tank, a liquid level detection device is further provided in the water supply tank, and a gas-liquid separation device is further provided on the hydrogen flow channel, the gas-liquid separation device delivering the separated water to the water supply tank.

10. The oxyhydrogen gas and hydrogen-rich water production system according to any one of claims 1 to 9, wherein the oxyhydrogen gas and hydrogen-rich water production system further comprises an intelligent control terminal, the intelligent control terminal comprises an intelligent AI chip and an internet of things control module, the intelligent AI chip is connected with the internet of things control module, and the hydrogen production module is connected with the internet of things control module.