CN109731202A - It can be to the water electrolysis hydrogen production oxygen breathing equipment that discharge hydrogen flows back - Google Patents
It can be to the water electrolysis hydrogen production oxygen breathing equipment that discharge hydrogen flows back Download PDFInfo
- Publication number
- CN109731202A CN109731202A CN201910106497.8A CN201910106497A CN109731202A CN 109731202 A CN109731202 A CN 109731202A CN 201910106497 A CN201910106497 A CN 201910106497A CN 109731202 A CN109731202 A CN 109731202A
- Authority
- CN
- China
- Prior art keywords
- gas
- flows back
- hydrogen
- discharge
- water
- Prior art date
- Legal status (The legal status 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 status listed.)
- Pending
Links
- 239000001257 hydrogen Substances 0.000 title claims abstract description 107
- 229910052739 hydrogen Inorganic materials 0.000 title claims abstract description 107
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims abstract description 102
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 85
- 239000001301 oxygen Substances 0.000 title claims abstract description 58
- 229910052760 oxygen Inorganic materials 0.000 title claims abstract description 58
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 title claims abstract description 54
- 238000005868 electrolysis reaction Methods 0.000 title claims abstract description 54
- 230000029058 respiratory gaseous exchange Effects 0.000 title claims abstract description 51
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 41
- 239000007789 gas Substances 0.000 claims abstract description 114
- 238000003860 storage Methods 0.000 claims abstract description 20
- 238000010992 reflux Methods 0.000 claims abstract description 19
- 238000006243 chemical reaction Methods 0.000 claims abstract description 13
- 238000001914 filtration Methods 0.000 claims abstract description 11
- 238000002360 preparation method Methods 0.000 claims abstract description 8
- 238000010790 dilution Methods 0.000 claims abstract description 4
- 239000012895 dilution Substances 0.000 claims abstract description 4
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 22
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 14
- 229910002092 carbon dioxide Inorganic materials 0.000 claims description 13
- 239000001569 carbon dioxide Substances 0.000 claims description 10
- 238000011084 recovery Methods 0.000 claims description 10
- 239000007788 liquid Substances 0.000 claims description 9
- 238000009792 diffusion process Methods 0.000 claims description 7
- 229910052757 nitrogen Inorganic materials 0.000 claims description 7
- 238000000926 separation method Methods 0.000 claims description 7
- 230000001105 regulatory effect Effects 0.000 claims description 5
- 238000001816 cooling Methods 0.000 claims description 4
- 238000007254 oxidation reaction Methods 0.000 claims description 4
- 239000013589 supplement Substances 0.000 claims description 4
- 230000003647 oxidation Effects 0.000 claims description 3
- 238000009736 wetting Methods 0.000 claims description 3
- 238000007664 blowing Methods 0.000 claims description 2
- 241000790917 Dioxys <bee> Species 0.000 claims 1
- 238000000889 atomisation Methods 0.000 claims 1
- 238000009298 carbon filtering Methods 0.000 claims 1
- 230000002209 hydrophobic effect Effects 0.000 description 12
- 239000012528 membrane Substances 0.000 description 10
- 239000000243 solution Substances 0.000 description 8
- 239000000463 material Substances 0.000 description 6
- 238000010586 diagram Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 150000002431 hydrogen Chemical class 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 230000005611 electricity Effects 0.000 description 3
- 238000005265 energy consumption Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 238000010248 power generation Methods 0.000 description 3
- 230000004888 barrier function Effects 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- 239000000919 ceramic Substances 0.000 description 2
- 239000008232 de-aerated water Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical group [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 208000004930 Fatty Liver Diseases 0.000 description 1
- 206010016654 Fibrosis Diseases 0.000 description 1
- 206010056328 Hepatic ischaemia Diseases 0.000 description 1
- 206010019708 Hepatic steatosis Diseases 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 239000004695 Polyether sulfone Substances 0.000 description 1
- 206010063837 Reperfusion injury Diseases 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- 229910000272 alkali metal oxide Inorganic materials 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 230000003078 antioxidant effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 210000000013 bile duct Anatomy 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 230000007882 cirrhosis Effects 0.000 description 1
- 208000019425 cirrhosis of liver Diseases 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000005474 detonation Methods 0.000 description 1
- 229910001882 dioxygen Inorganic materials 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 230000001815 facial effect Effects 0.000 description 1
- 208000010706 fatty liver disease Diseases 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 229920002313 fluoropolymer Polymers 0.000 description 1
- 208000006454 hepatitis Diseases 0.000 description 1
- 231100000283 hepatitis Toxicity 0.000 description 1
- 230000008595 infiltration Effects 0.000 description 1
- 238000001764 infiltration Methods 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 208000019423 liver disease Diseases 0.000 description 1
- 239000002923 metal particle Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910000510 noble metal Inorganic materials 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 229920000620 organic polymer Polymers 0.000 description 1
- 238000002640 oxygen therapy Methods 0.000 description 1
- 229920002239 polyacrylonitrile Polymers 0.000 description 1
- 229920006393 polyether sulfone Polymers 0.000 description 1
- 239000002861 polymer material Substances 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 238000003892 spreading Methods 0.000 description 1
- 231100000240 steatosis hepatitis Toxicity 0.000 description 1
- 230000001225 therapeutic effect Effects 0.000 description 1
- 210000003437 trachea Anatomy 0.000 description 1
- 210000005239 tubule Anatomy 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
Classifications
-
- 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
Landscapes
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Abstract
It, more particularly, to can be to the water electrolysis hydrogen production oxygen breathing equipment that discharge hydrogen flows back the invention belongs to be electrolysed the technical field of manufacture hydrogen and oxygen.Including water storage container, electrolysis unit, the electrolysis unit is equipped with the first escape pipe for the oxygen outflow for preparation, and the second escape pipe for the hydrogen outflow for preparation, first escape pipe is connected to after collecting with the second escape pipe with gas delivery port, and breathing nozzle is also connected at the gas delivery port, the gas return conduit of gas backstreaming at nozzle will be breathed when being additionally provided at the breathing nozzle for exhaling to user, the processing unit for carrying out reaction filtration treatment and/or dilution discharge to reflux gas is also connected on the gas return conduit, and the breathing nozzle and gas return conduit are all connected on respirator.Increase gas return conduit on respirator, so that user flows back the gas of gas and exhalation that device generates when exhaling.
Description
[technical field]
The invention belongs to be electrolysed the technical field of manufacture hydrogen and oxygen, discharge hydrogen can more particularly, to be returned
The water electrolysis hydrogen production oxygen breathing equipment of stream.
[background technique]
Studies show that, hydrogen is as a kind of selective antioxidant, hydrogen is to hepatic ischemia/reperfusion injury, drug hepatitis, bile duct
A plurality of types of liver diseases such as cirrhosis, fatty liver caused by blocking have effective and apparent therapeutic effect.Market at present
On released the products such as hydrogen manufacturing cup, to facilitate people in daily middle intake hydrogen.
Currently, oxy-hydrogen breathing machine, hydrogen-oxygen generating apparatus on the market, after producing hydrogen and oxygen, directly for using
Person draws, and user is in exhalation, and high concentration of hydrogen oxygen gas mixture is usually directly exported into air, or is gathered in and is made
Near user's face, great security risk is brought to consumer.
[summary of the invention]
To solve to be easy to cause user's facial surroundings hydrogen concentration in use process in hydrogen-oxygen generating apparatus in the prior art
The problem of raising, the present invention provides can be to the water electrolysis hydrogen production oxygen breathing equipment that discharge hydrogen flows back.
The present invention is achieved by the following technical solutions:
It can be to the water electrolysis hydrogen production oxygen breathing equipment that discharge hydrogen flows back, including water storage container and the water storage
The electrolysis unit of container connection, the electrolysis unit are equipped with the first escape pipe, Yi Jiyong for the oxygen outflow for preparation
In the second escape pipe of the hydrogen outflow for preparation, first escape pipe and the second escape pipe collect rear and gas delivery port and connect
It is logical, and breathing nozzle is also connected at the gas delivery port, when being additionally provided at the breathing nozzle for exhaling to user
The gas return conduit that gas backstreaming at nozzle will be breathed, be also connected on the gas return conduit for reflux gas into
The processing unit of row reaction filtration treatment and/or dilution discharge, and the breathing nozzle and gas return conduit are both connected to
On respirator.
Can be to the water electrolysis hydrogen production oxygen breathing equipment that discharge hydrogen flows back, the processing unit as described above
Booster fan on gas return conduit for reflux gas to be pressurized is set.
It as described above can be to the water electrolysis hydrogen production oxygen breathing equipment that discharge hydrogen flows back, the processing unit packet
It includes on gas return conduit for the reaction filter core by oxidation of hydrogen for water.
It as described above can be to the water electrolysis hydrogen production oxygen breathing equipment that flows back of discharge hydrogen, on the reaction filter core
It is additionally provided with air supplement entrance, air discharge entrance, is additionally provided with drainage pipeline, the drainage pipeline is connected to water storage container.
It as described above can be to the water electrolysis hydrogen production oxygen breathing equipment that discharge hydrogen flows back, the processing unit packet
Including can the nitrogen separation device to nitrogen filtering in gas recovery and the carbon dioxide filtering to carbon dioxide filtering in gas recovery
Device.
It as described above can be to the water electrolysis hydrogen production oxygen breathing equipment that discharge hydrogen flows back, the gas delivery port
Place is also connected with gas diffusion nozzle, and the gas diffusion nozzle is also connected with blower, and there are two the air inlets of the blower,
In one for close to the electrolysis unit, and air inlet described in two goes out to be equipped with regulating switch, is additionally provided on the blower
Supersonic atomizer for the air wetting blown out to it.
It as described above can be to the water electrolysis hydrogen production oxygen breathing equipment that discharge hydrogen flows back, the gas backstreaming pipe
The one end in road is connected to respirator, and the other end is opened on equipment cooling fan.
It as described above can be to the water electrolysis hydrogen production oxygen breathing equipment that discharge hydrogen flows back, first escape pipe
On be connected to the first moisture trap, be connected to the second moisture trap on second escape pipe, first moisture trap with
Gas outlet duct on second moisture trap is connected to after converging with the gas delivery port.It is additionally provided on the water storage container
Reflux line, first moisture trap are connected to the liquid outlet on the second moisture trap with reflux line, and even
Logical place is additionally provided with the porous filter screen made of poromerics.
It as described above can be to the water electrolysis hydrogen production oxygen breathing equipment that discharge hydrogen flows back, first air water point
From being additionally provided with filter on the gas outlet duct of device.
It as described above can be to the water electrolysis hydrogen production oxygen breathing equipment that discharge hydrogen flows back, first air water point
From the gas outlet duct meet on device and the second moisture trap and humidification bottle is further connected between gas delivery port.
Compared with prior art, the present invention has the following advantages:
1, the present invention provides can be to the water electrolysis hydrogen production oxygen breathing equipment that discharge hydrogen flows back, on respirator
Increase gas return conduit, so that user flows back the gas of gas and exhalation that device generates when exhaling.This
Sample one is directly discharged to user's face nearby can be avoided hydrogen that device produces and oxygen, two it is subsequent can to time
The gas of stream is reprocessed, is flowed back again with (such as power generation, separation N2、CO2Reuse afterwards etc.), so that reducing the device makes
The security risk present in process, and save the energy consumption that hydrogen and oxygen are produced.
2, the present invention can to the water electrolysis hydrogen production oxygen breathing equipment that flows back of discharge hydrogen, by booster fan or
Reflux gas is dispelled rear direct emission or by discharge of pipes to home by the included radiator fan of person's device, in this way
The device can be solved by simple structure setting and there is the security risk for discharging high concentration hydrogen near user's face.
3, the present invention can be to the water electrolysis hydrogen production oxygen breathing equipment that discharge hydrogen flows back, can also be by reacting filter core
By the hydrogen in reflux gas carry out reaction become water, hydrogen treat can so be fallen, two come by by water back to
In water storage container, realizes and recycle.
[Detailed description of the invention]
To describe the technical solutions in the embodiments of the present invention more clearly, make required in being described below to embodiment
Attached drawing is briefly described, it should be apparent that, drawings in the following description are only some embodiments of the invention, for
For those of ordinary skill in the art, without creative efforts, it can also be obtained according to these attached drawings other
Attached drawing.
Fig. 1 is that the present invention can be to the schematic diagram for the water electrolysis hydrogen production oxygen breathing equipment that discharge hydrogen flows back；
Fig. 2 is that the present invention (can scheme the schematic diagram two for the water electrolysis hydrogen production oxygen breathing equipment that discharge hydrogen flows back
Middle omission diffuser)；
Fig. 3 is embodiment schematic diagram of the processing unit of the present invention only with fan air-heater；
Fig. 4 is the schematic diagram one of processing device embodiment three of the present invention；
Fig. 5 is the schematic diagram two of processing device embodiment three of the present invention.
[specific embodiment]
In order to which the technical problems, technical solutions and beneficial effects solved by the present invention is more clearly understood, below in conjunction with
Accompanying drawings and embodiments, the present invention will be described in further detail.It should be appreciated that specific embodiment described herein is only used
To explain the present invention, it is not intended to limit the present invention.
The present invention is achieved by the following technical solutions:
As shown in Figure 1, can to the water electrolysis hydrogen production oxygen breathing equipment that flows back of discharge hydrogen, including water storage container 1,
The electrolysis unit 2 connecting with the water storage container 1, the electrolysis unit 2 are equipped with first for the oxygen outflow for preparation
Escape pipe 31 and the second escape pipe 32 flowed out for the hydrogen for preparation, first escape pipe 31 and the second escape pipe
32 collect after be connected to gas delivery port 5, and be also connected at the gas delivery port 5 breathe nozzle 81, the breathing nozzle
The gas return conduit 83 of gas backstreaming at nozzle 81 will be breathed when being additionally provided at 81 for exhaling to user, the gas returns
The processing unit for carrying out reaction filtration treatment and/or dilution discharge to reflux gas, and institute are also connected on flow tube road 83
It states breathing nozzle 81 and gas return conduit 83 is all connected on respirator.The present invention provides can return to discharge hydrogen
The water electrolysis hydrogen production oxygen breathing equipment of stream, increases gas return conduit on respirator, so that user will dress when exhaling
The gas of the gas and exhalation of setting generation flows back.So it can be avoided hydrogen that device produces and oxygen be direct
Be emitted into user face nearby, two it is subsequent the gas of reflux can be reprocessed, flow back again with (as power generation, separate
Reused after N2, CO2 etc.), to reduce the device existing security risk in use, and save hydrogen and oxygen
The energy consumption that gas is produced.
In addition, respirator can in this programme to achieve the effect that above-mentioned user gas return conduit when exhaling is opened
It can be realized using the scheme as disclosed in patent " breathing equipment of controllable tolerance " (application No. is 2017217390140).Its
It is no longer explained in specific structure this programme.
Further, the processing unit is arranged on gas return conduit 83 for dispelling reflux gas pressurization
Booster fan 91.It is discharged into other places after dispelling reflux gas by booster fan, passes through simple structure setting in this way
It can reach the hydrogen concentration for reducing user's surrounding air.
Moreover, as shown in figure 3, optimization as above scheme, one end of the gas return conduit 83 is connected to breathing
Device, the other end are opened on equipment cooling fan.Force(d) (draft) fan of the cooling fan carried by device as above scheme, also can
Reach identical effect.And enable to apparatus structure more simple.In addition, can by the fan Hot-air fan that the device carries
Directly gas recovery is discharged, and discharge outlet General Principle user, in addition discharge tube can also be set gas recovery is arranged
It puts.It can be arranged according to the occasion used, such as personal use is not required to that discharge tube is separately provided；Such as in oxygen therapy room, then preferably
Pass through discharge tube uniform effluent to outdoor.
In addition, as shown in Fig. 2, the processing unit includes on gas return conduit 83 for being by oxidation of hydrogen
The reaction filter core 92 of water is additionally provided with air supplement entrance, air discharge entrance on the reaction filter core 92.Filter core 92 is reacted to use
The micropore film material that platinum group noble metal makees catalyst is made；The oxidation reaction to hydrogen is realized by catalyst.And it is
The content for supplying oxygen, specially opens up air supply port and air discharge ports, can also by the wind pressure such as blower equipment come from
Extract enough air in the external world.
Specifically, hydrogen and oxygen reacts when contacting platinum group metal particle when passing through micropore filtrate, and generation heat/
Electricity and water, electricity and water can recycle, and heat can drive air to supplement and discharge.This filter core can be made tabular,
Tubulose or film wire shape, material can be ceramics, organic polymer.The size of micropore is preferably 1mm or less.
Moreover, the reaction filter core 92 is additionally provided with drainage pipeline 93, the drainage pipeline 93 is connected to water storage container 1.It is logical
It crosses the water of reaction generation back to water storage container to realize that recycling, simple structure are increased operation rate.
Still further, the embodiment three of processing unit, the processing unit includes can be to nitrogen filtering in gas recovery
Nitrogen separation device 94 and in gas recovery carbon dioxide filter carbon dioxide filter 95.Sieve technology can be used
Separation and discharge nitrogen are retained hydrogen and oxygen and are breathed for user using alkali metal oxide or the fixed carbon dioxide of solution.Such as
Shown in Fig. 4, carbon dioxide filter is carbon dioxide chemistry adsorbent equipment in the program.As shown in figure 5, carbon dioxide filter
For carbon dioxide molecule sieve.And in processing unit further include for by filtered gas recovery back to the circulation on breath device
Pipeline 96.
Further, gas diffusion nozzle 82, the gas diffusion nozzle 82 are also connected at the gas delivery port 5
It is also connected with blower 9, there are two the air inlets of the blower 9, one of them is close to the electrolysis unit 2.The present invention provides
It can be to the water electrolysis hydrogen production oxygen breathing equipment that discharge hydrogen flows back, in order to enable mixed gas directly for user
It exhales, normal air or filtered air is passed through by blower, to reduce the concentration of hydrogen-oxygen in mixed gas, be easy to use
Person, which breathes, to be used.When hydrogen and oxygen breathe, mixed proportion 2:1 has some potential safety problems.Here design has blower
And diffusion trachea, delivery air, the hydrogen being nearby enriched with for dispelling body respirator avoid bringing after density of hydrogen is excessively high
Detonation risk.And the air inlet of the blower has 2, and one of them is close to electrolysis unit, another air inlet and ring
Close at the temperature of border, one is located at cell attachment (hot-air), and one is located at environment temperature (normal temperature air), then can be with
Alternative selection uses, even if returning user in cold winter in this way and providing warm breathing gas.In this programme
In, heat that the Selection utilization electrolysis unit more optimized generates during startup, blower is taking the partial heat out of
Meanwhile also acting as heat spreading function.
Further, air inlet described in two, which goes out, is equipped with regulating switch.So that this product can also by adjust 2 into
The intake in air port carries out the adjusting of temperature.Intake is controlled by the openings of sizes of 2 regulating switches, to adjust heat
The mixed proportion of air and normal temperature air come realize temperature adjust.It is real that battery valve can be used in regulating switch described in this programme
It is existing.
Further, the supersonic atomizer of the air wetting for blowing out to it is additionally provided on the blower 9.It is logical
Crossing supersonic atomizer can be improved humidity in air, further allow user to use more comfortable.
Further, the first moisture trap 41 is connected on first escape pipe 31, on second escape pipe 32
It is connected to the second moisture trap 42, the gas outlet duct on first moisture trap 41 and the second moisture trap 42 converges
It is connected to after conjunction with the gas delivery port 5.It, can be straight after being separated by moisture trap since the gas produced all has moisture
It connects for human body respiration, moreover, tradition machinery formula separator can be used in moisture trap.And in the present solution, first escape pipe
It is connected to the first moisture trap 41 with hydrophobic permeable membrane on 31, is connected on second escape pipe 32 with hydrophobic permeable membrane
The second moisture trap 42, first moisture trap 41 converges with the gas outlet duct on the second moisture trap 42
It is connected to afterwards with gas delivery port 5.It carries out electrolysis to the water imported in water storage container by electrolysis unit and produces hydrogen
Water and oxygenous water after, after the first outlet pipe and the output of the second outlet pipe type, be directed respectively into using having
Have and be filtered moisture in the moisture trap of hydrophobic permeable membrane, last dewatered gas is exported from gas output tube to equipment
Gas delivery port.Wherein gas separator is filtered the steam in gas using hydrophobic permeable membrane, and structure is simple, and
And good separating effect, so that equipment volume is reduced, convenient for using on respirator.
In the present solution, hydrophobic permeable membrane is specifically, the hydrophobic permeable membrane in first moisture trap 41 is using poly-
The parents such as microporous barrier made of alkene, fluorinated polymer material, or polyether sulfone, polyacrylonitrile, ceramics of the use Jing Guo hydrophobic treatment
Microporous barrier made of water material.It preferentially chooses less than 0.2 micron in its aperture.
Hydrophobic permeable membrane in first moisture trap 41 can be made into cortina shape stereoscopic film.Certainly using hydrophobic permeable membrane
The ventilative attribute of body adds stereochemical structure, while capable of efficiently separating air water, prevents steam from investing film surface and causes to block up
Plug.Its principle is, in the state of steam, particle water is very tiny, according to the principle of capillary moving, can smoothly penetrate into hair
Tubule is to the other side, so that vapour phenomenon occur.After moisture condensation becomes droplet, particle becomes larger, due to droplet surface tension
Effect (mutual " pull and contend with " between hydrone), hydrone cannot smoothly be detached from droplet and penetrate into the other side, that is,
It prevents the infiltration of water to occur, steam film is made to have hydrophobic function.
In addition, following material can also be used, the hydrophobic permeable membrane in first moisture trap 41 is hydrophobic type micropore
Material is made, and aperture is less than 10 microns thereon.Pp or pbdf may be selected in material, and aperture is preferentially chosen less than 0.2 micron.Its
Has the effect of preferable steam separation.
In addition, reflux line 11 is additionally provided on the water storage container 1, first moisture trap 41 and the second air water point
It is connected to from the liquid outlet on device 42 with reflux line 11, and connectivity part is additionally provided with the porous filter screen made of poromerics
43.Liquid after being separated by moisture trap can be flow back into water storage container by reflux line, realize Recycling.And
And also by increasing porous filter screen, the liquid (hereinafter referred to as de aerated water) after separating by moisture trap, de aerated water exit
By porous filter screen 43, micro-bubble in water body is collected, and making minute bubbles convergence be air pocket (is the gas of manufacture in bubble
Body), certain compartmentation is also functioned to, that is, the collection efficiency of gas can be improved.Moreover, in the present solution, the aperture of porous filter screen
Preferential >=0.1 micron of selection.
Moreover, being additionally provided with filter 6 on the gas outlet duct of first moisture trap 41.Work can be used in filter
Property charcoal filtering, the ozone ingredient that may contain in the oxygen of main filtration manufacture.
In addition, first moisture trap 41 and gas outlet duct meet and gas on the second moisture trap 42
Humidification bottle 7 is further connected between body delivery outlet 5.Increase humidification bottle 7 the humidity in mixed gas can be improved, so that user inhales
It takes more comfortable；Two, come due to containing hydrogen in mixed gas, being somebody's turn to do is explosive inflammable gas, can prevent gas after increasing humidity
It is inflammable, improve security performance.
Moreover, being additionally provided with pressure sensor between second escape pipe 32 and second moisture trap 42.Work as electricity
After solving device starting, can detect whether to be electrolysed the hydrogen generated after successfully successfully starting up by pressure sensor leads to second
The variation of outlet pipe internal gas.
Similarly, also hydrogen gas sensor can be set outside present apparatus pipeline, is used in detection device whether have hydrogen leak,
Avoid the danger exploded caused by because of leakage.
Also further, in order to enable this equipment is more intelligent, conveniently, liquid level sensor can be increased in water storage container,
It can be detected in time and user adds water into water storage container.
Specifically, this equipment is ventilator, and gas delivery port is the exhalation vents directly drawn for user thereon.And this
Electrolysis unit can be used conventional SPE membrane technology and realize that electrolysis and hydrogen-oxygen shunt.
Also further, the electrolysis unit 2 includes the electrolytic cell with SPE film, and the electrolytic cell is located at the two sides of film
Left water inlet and right water inlet are respectively equipped on each, and the left water inlet is connected to right water inlet by a connecting pipe 21,
It is also connected with liquid output pipe road 33 on second escape pipe 32, on the liquid output pipe road 33 and connecting pipe 21
Equipped with switch valve, switch valve described in two can open or close simultaneously.The present invention provides the electrolysis waters of exportable hydrogeneous water
Hydrogen and oxygen production equipment be electrolysed the water for producing hydrogen and contain to the water imported in water storage container by electrolysis unit
It after the water of oxygen, is exported by the first outlet pipe and the second outlet pipe type, and behind increase liquid output pipe road, can increased
Add the function of the hydrogeneous water of this device fabrication, can directly export hydrogeneous water carry out using, user can by open the switch valve into
Row selection.
The present invention provides can increase on respirator to the water electrolysis hydrogen production oxygen breathing equipment that discharge hydrogen flows back
Add gas return conduit, so that user flows back the gas of gas and exhalation that device generates when exhaling.In this way
One is directly discharged near user's face can be avoided hydrogen that device produces and oxygen, two it is subsequent can be to reflux
Gas reprocessed, flow back again with (as power generation, separation N2、CO2Reuse afterwards etc.), it is being used to reduce the device
Existing security risk in the process, and save the energy consumption that hydrogen and oxygen are produced.
It is the one or more embodiments provided in conjunction with particular content as described above, does not assert specific reality of the invention
It applies and is only limited to these instructions.It is all approximate with method of the invention, structure etc., identical, or for present inventive concept under the premise of
It makes several technologies to deduce, or replacement all should be considered as protection scope of the present invention.
Claims (10)
1. can be to the water electrolysis hydrogen production oxygen breathing equipment that discharge hydrogen flows back, which is characterized in that including water storage container
(1), the electrolysis unit (2) connecting with the water storage container (1), the electrolysis unit (2) are equipped with for the oxygen for preparation
The first escape pipe (31) of outflow and the second escape pipe (32) flowed out for the hydrogen for preparation, first escape pipe
(31) it is connected to after collecting with the second escape pipe (32) with gas delivery port (5), and is also connected with and exhales at the gas delivery port (5)
Suction pipe mouth (81), will gas backstreaming at breathing nozzle (81) when being additionally provided with for exhaling to user at the breathing nozzle (81)
Gas return conduit (83), be also connected on the gas return conduit (83) for being carried out at reaction filtering to reflux gas
The processing unit of reason and/or dilution discharge, and the breathing nozzle (81) and gas return conduit (83) are both connected to breathing
On device.
2. according to claim 1 can be to the water electrolysis hydrogen production oxygen breathing equipment that discharge hydrogen flows back, feature
It is, the processing unit is the booster fan (91) being arranged on gas return conduit (83) for reflux gas to be pressurized.
3. according to claim 1 or described in 2 can to the water electrolysis hydrogen production oxygen breathing equipment that discharge hydrogen flows back,
It is characterized in that, the processing unit includes on gas return conduit (83) for the reaction filter core by oxidation of hydrogen for water
(92)。
4. according to claim 3 can be to the water electrolysis hydrogen production oxygen breathing equipment that discharge hydrogen flows back, feature
It is, air supplement entrance, air discharge entrance is additionally provided on the reaction filter core (92), is additionally provided with drainage pipeline (93), institute
It states drainage pipeline (93) and is connected to water storage container (1).
5. according to claim 1 can be to the water electrolysis hydrogen production oxygen breathing equipment that discharge hydrogen flows back, feature
It is, the processing unit includes can nitrogen separation device (94) to nitrogen filtering in gas recovery and to dioxy in gas recovery
Change the carbon dioxide filter (95) of carbon filtering, and in processing unit further include for by filtered gas recovery back to exhaling
Circulating line on gas device.
6. according to claim 1 can be to the water electrolysis hydrogen production oxygen breathing equipment that discharge hydrogen flows back, feature
It is, be also connected with gas diffusion nozzle (82) at the gas delivery port (5), the gas diffusion nozzle (82) is also connected with
Blower (9), there are two the air inlets of the blower (9), one of them is close the electrolysis unit (2), and described in two
Air inlet goes out to be equipped with regulating switch, and the ultrasonic atomization of the air wetting for blowing out to it is additionally provided on the blower (9)
Device.
7. according to claim 1 can be to the water electrolysis hydrogen production oxygen breathing equipment that discharge hydrogen flows back, feature
It is, one end of the gas return conduit (83) is connected to respirator, and the other end is opened on equipment cooling fan.
8. according to claim 4 can be to the water electrolysis hydrogen production oxygen breathing equipment that discharge hydrogen flows back, feature
It is, is connected to the first moisture trap (41) on first escape pipe (31), is connected to second on second escape pipe (32)
Moisture trap (42), first moisture trap (41) are converged with the gas outlet duct on the second moisture trap (42)
It is connected to afterwards with the gas delivery port (5).It is additionally provided with reflux line (11) on the water storage container (1), first air water point
Be connected to the liquid outlet on the second moisture trap (42) with reflux line (11) from device (41), and connectivity part be additionally provided with by
Porous filter screen made of poromerics.
9. according to claim 8 can be to the water electrolysis hydrogen production oxygen breathing equipment that discharge hydrogen flows back, feature
It is, is additionally provided with filter (6) on the gas outlet duct of first moisture trap (41).
10. according to claim 8 can be to the water electrolysis hydrogen production oxygen breathing equipment that discharge hydrogen flows back, feature
Be, first moisture trap (41) on the second moisture trap (42) gas outlet duct meet and gas it is defeated
Humidification bottle (7) are further connected between outlet (5).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910106497.8A CN109731202A (en) | 2019-02-02 | 2019-02-02 | It can be to the water electrolysis hydrogen production oxygen breathing equipment that discharge hydrogen flows back |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910106497.8A CN109731202A (en) | 2019-02-02 | 2019-02-02 | It can be to the water electrolysis hydrogen production oxygen breathing equipment that discharge hydrogen flows back |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN109731202A true CN109731202A (en) | 2019-05-10 |
Family
ID=66367253
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910106497.8A Pending CN109731202A (en) | 2019-02-02 | 2019-02-02 | It can be to the water electrolysis hydrogen production oxygen breathing equipment that discharge hydrogen flows back |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN109731202A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110639137A (en) * | 2019-09-23 | 2020-01-03 | 宁波市欣宁信息科技有限公司 | Oxygen supply device and method based on electrolyzed water |
| CN111658926A (en) * | 2020-06-16 | 2020-09-15 | 山东卫康生物医药科技有限公司 | Preparation method of hydrogen absorption machine |
| CN111701132A (en) * | 2020-06-01 | 2020-09-25 | 云南新益新能源有限公司 | Oxyhydrogen breathing machine with heating atomization medicine |
| CN113073338A (en) * | 2021-03-19 | 2021-07-06 | 深圳市创辉氢科技发展有限公司 | Electrolytic cell |
| CN113559385A (en) * | 2021-09-01 | 2021-10-29 | 安波澜(北京)医疗设备有限公司 | Gas circuit structure of hydrogen breathing machine |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2326590Y (en) * | 1997-12-21 | 1999-06-30 | 吕铁平 | Oxygen generator for breathing |
| JP2003013269A (en) * | 2001-07-03 | 2003-01-15 | Norio Kihara | System and method for supplying oxygen |
| CN105163788A (en) * | 2013-09-01 | 2015-12-16 | 河村隆夫 | Hydrogen-rich gas mixture breathing system |
| WO2017149684A1 (en) * | 2016-03-01 | 2017-09-08 | 株式会社グレイトチレン | Wet high-concentration hydrogen-mixed-gas respiration system |
| CN108310561A (en) * | 2018-01-30 | 2018-07-24 | 东莞市美氢源生物科技有限公司 | A kind of hydrogen lung ventilator |
| CN210057076U (en) * | 2019-02-02 | 2020-02-14 | 张建国 | Water electrolysis hydrogen production and oxygen production breathing device capable of refluxing discharged hydrogen |
-
2019
- 2019-02-02 CN CN201910106497.8A patent/CN109731202A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2326590Y (en) * | 1997-12-21 | 1999-06-30 | 吕铁平 | Oxygen generator for breathing |
| JP2003013269A (en) * | 2001-07-03 | 2003-01-15 | Norio Kihara | System and method for supplying oxygen |
| CN105163788A (en) * | 2013-09-01 | 2015-12-16 | 河村隆夫 | Hydrogen-rich gas mixture breathing system |
| WO2017149684A1 (en) * | 2016-03-01 | 2017-09-08 | 株式会社グレイトチレン | Wet high-concentration hydrogen-mixed-gas respiration system |
| CN108310561A (en) * | 2018-01-30 | 2018-07-24 | 东莞市美氢源生物科技有限公司 | A kind of hydrogen lung ventilator |
| CN210057076U (en) * | 2019-02-02 | 2020-02-14 | 张建国 | Water electrolysis hydrogen production and oxygen production breathing device capable of refluxing discharged hydrogen |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110639137A (en) * | 2019-09-23 | 2020-01-03 | 宁波市欣宁信息科技有限公司 | Oxygen supply device and method based on electrolyzed water |
| CN110639137B (en) * | 2019-09-23 | 2021-05-11 | 宁波市欣宁信息科技有限公司 | Oxygen supply device and method based on electrolyzed water |
| CN111701132A (en) * | 2020-06-01 | 2020-09-25 | 云南新益新能源有限公司 | Oxyhydrogen breathing machine with heating atomization medicine |
| CN111658926A (en) * | 2020-06-16 | 2020-09-15 | 山东卫康生物医药科技有限公司 | Preparation method of hydrogen absorption machine |
| CN113073338A (en) * | 2021-03-19 | 2021-07-06 | 深圳市创辉氢科技发展有限公司 | Electrolytic cell |
| CN113559385A (en) * | 2021-09-01 | 2021-10-29 | 安波澜(北京)医疗设备有限公司 | Gas circuit structure of hydrogen breathing machine |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN109731202A (en) | It can be to the water electrolysis hydrogen production oxygen breathing equipment that discharge hydrogen flows back | |
| CN209873126U (en) | Hydrogen and oxygen production equipment capable of simultaneously outputting hydrogen-containing water and hydrogen-oxygen mixed gas | |
| CN109966666A (en) | A kind of portable air purifier for resisting haze | |
| CN210057076U (en) | Water electrolysis hydrogen production and oxygen production breathing device capable of refluxing discharged hydrogen | |
| CN107518473A (en) | A kind of intelligent atomization mouth mask | |
| CN210314506U (en) | Hydrogen-oxygen mixed gas for hydrogen production and oxygen production by electrolysis and hydrogen-containing water breathing drinking device | |
| CN208990101U (en) | A kind of water mist upgraded carbon-oxygen crossover autonomous respiration device | |
| CN209611941U (en) | A kind of oral cavity warming humidification device | |
| CN206675798U (en) | A kind of oxygen cycle ventilator mask | |
| CN203829285U (en) | Novel rhinitis fumigator | |
| CN206433817U (en) | It is a kind of split type to produce oxygen-enriched, negative oxygen ion anti-dust respirator | |
| CN102151351B (en) | Portable oxygen source supply device applicable to anaesthesia apparatus or breathing machine | |
| CN108273207A (en) | Novel breath purifying device and Novel respirator | |
| CN108354816A (en) | A kind of novel facial vaporizer of energy releasing negative oxygen ion | |
| CN208852277U (en) | Novel breath purifying device and Novel respirator | |
| CN210065940U (en) | Hydrogen and oxygen producing apparatus by electrolyzing water | |
| CN208355883U (en) | A kind of new medicine aromatic odor therapy device | |
| CN213491349U (en) | Self-moistening humidification anti-drying anti-cold breathing auxiliary device | |
| CN212466778U (en) | Portable atomizing breathing machine | |
| CN203694299U (en) | Breathing machine | |
| KR200384033Y1 (en) | Oxygen generating air purifier | |
| CN205268777U (en) | Breathe internal medicine oxygen therapy auxiliary device | |
| CN216366215U (en) | Multifunctional portable oxyhydrogen machine | |
| CN215231207U (en) | Adjustable atomizing mask for pediatric respiratory therapy | |
| CN213454064U (en) | Remove peculiar smell air purification filter |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination |