CN109082679A - Gas generator - Google Patents
Gas generator Download PDFInfo
- Publication number
- CN109082679A CN109082679A CN201810941576.6A CN201810941576A CN109082679A CN 109082679 A CN109082679 A CN 109082679A CN 201810941576 A CN201810941576 A CN 201810941576A CN 109082679 A CN109082679 A CN 109082679A
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- Prior art keywords
- water
- water tank
- electrolysis
- hydrogen
- electrolysis unit
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Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 488
- 238000005868 electrolysis reaction Methods 0.000 claims abstract description 315
- 239000007789 gas Substances 0.000 claims abstract description 196
- 239000001301 oxygen Substances 0.000 claims abstract description 20
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 20
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 136
- 239000001257 hydrogen Substances 0.000 claims description 136
- 229910052739 hydrogen Inorganic materials 0.000 claims description 136
- 239000000203 mixture Substances 0.000 claims description 125
- 229910001882 dioxygen Inorganic materials 0.000 claims description 120
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 claims description 119
- 238000000889 atomisation Methods 0.000 claims description 60
- 238000005086 pumping Methods 0.000 claims description 56
- 238000002156 mixing Methods 0.000 claims description 45
- 210000005056 cell body Anatomy 0.000 claims description 40
- 239000013589 supplement Substances 0.000 claims description 32
- 230000036541 health Effects 0.000 claims description 19
- 239000003814 drug Substances 0.000 claims description 5
- 239000007788 liquid Substances 0.000 claims description 5
- 235000015096 spirit Nutrition 0.000 claims description 3
- 238000013461 design Methods 0.000 abstract description 34
- 238000004880 explosion Methods 0.000 abstract description 15
- 238000001816 cooling Methods 0.000 description 27
- 238000010586 diagram Methods 0.000 description 20
- 238000001914 filtration Methods 0.000 description 18
- 238000005192 partition Methods 0.000 description 15
- 239000012535 impurity Substances 0.000 description 12
- 239000011148 porous material Substances 0.000 description 12
- NJPPVKZQTLUDBO-UHFFFAOYSA-N novaluron Chemical compound C1=C(Cl)C(OC(F)(F)C(OC(F)(F)F)F)=CC=C1NC(=O)NC(=O)C1=C(F)C=CC=C1F NJPPVKZQTLUDBO-UHFFFAOYSA-N 0.000 description 10
- 239000003792 electrolyte Substances 0.000 description 9
- 230000000694 effects Effects 0.000 description 7
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 6
- 230000005611 electricity Effects 0.000 description 6
- 239000000463 material Substances 0.000 description 6
- QFAXIZQBSCGJMA-UHFFFAOYSA-N mercury;hydrate Chemical compound O.[Hg] QFAXIZQBSCGJMA-UHFFFAOYSA-N 0.000 description 6
- 238000009833 condensation Methods 0.000 description 5
- 230000005494 condensation Effects 0.000 description 5
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 5
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 4
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 4
- 230000008901 benefit Effects 0.000 description 4
- 238000001514 detection method Methods 0.000 description 4
- 201000010099 disease Diseases 0.000 description 4
- 230000008859 change Effects 0.000 description 3
- 239000002360 explosive Substances 0.000 description 3
- 230000017525 heat dissipation Effects 0.000 description 3
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical class C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 3
- 150000003254 radicals Chemical class 0.000 description 3
- 208000017667 Chronic Disease Diseases 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 208000027418 Wounds and injury Diseases 0.000 description 2
- 230000003712 anti-aging effect Effects 0.000 description 2
- 238000013459 approach Methods 0.000 description 2
- 229910000019 calcium carbonate Inorganic materials 0.000 description 2
- 230000008878 coupling Effects 0.000 description 2
- 238000010168 coupling process Methods 0.000 description 2
- 238000005859 coupling reaction Methods 0.000 description 2
- 230000006378 damage Effects 0.000 description 2
- 238000004090 dissolution Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000011049 filling Methods 0.000 description 2
- 208000014674 injury Diseases 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 239000011244 liquid electrolyte Substances 0.000 description 2
- 210000004072 lung Anatomy 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000003595 mist Substances 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 239000011780 sodium chloride Substances 0.000 description 2
- 239000008400 supply water Substances 0.000 description 2
- 229910001316 Ag alloy Inorganic materials 0.000 description 1
- 229910000838 Al alloy Inorganic materials 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 229910000881 Cu alloy Inorganic materials 0.000 description 1
- 229910001021 Ferroalloy Inorganic materials 0.000 description 1
- 208000026350 Inborn Genetic disease Diseases 0.000 description 1
- 206010028980 Neoplasm Diseases 0.000 description 1
- 239000004113 Sepiolite Substances 0.000 description 1
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 239000004411 aluminium Substances 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 230000003064 anti-oxidating effect Effects 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 230000003078 antioxidant effect Effects 0.000 description 1
- 235000006708 antioxidants Nutrition 0.000 description 1
- 230000003796 beauty Effects 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- 201000011510 cancer Diseases 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 210000004027 cell Anatomy 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 238000002512 chemotherapy Methods 0.000 description 1
- 230000009514 concussion Effects 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 238000012937 correction Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 230000037213 diet Effects 0.000 description 1
- 235000005911 diet Nutrition 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 208000016361 genetic disease Diseases 0.000 description 1
- 235000013402 health food Nutrition 0.000 description 1
- 239000011796 hollow space material Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000002075 main ingredient Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000010453 quartz Substances 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 230000029058 respiratory gaseous exchange Effects 0.000 description 1
- 238000012216 screening Methods 0.000 description 1
- 229910052624 sepiolite Inorganic materials 0.000 description 1
- 235000019355 sepiolite Nutrition 0.000 description 1
- 229910052709 silver Inorganic materials 0.000 description 1
- 239000004332 silver Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 230000001502 supplementing effect Effects 0.000 description 1
- 208000024891 symptom Diseases 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
- 230000000007 visual effect Effects 0.000 description 1
- 239000000341 volatile oil 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
Abstract
The invention discloses a gas generator, which comprises a water tank and an electrolysis device. The water tank has a first hollow portion containing electrolyzed water. The electrolysis device is arranged in the first hollow part of the water tank and is used for electrolyzing the electrolyzed water to generate hydrogen-oxygen mixed gas. When the electrolysis device is operated, the water level of the electrolyzed water in the first hollow part is between 90 percent and 100 percent of the full water level. The gas generator of the invention provides a space-saving primary-secondary design, and simultaneously reduces the possibility of gas explosion of the hydrogen-oxygen mixed gas through the design of a near zero gas cavity.
Description
The application be the applying date be on November 05th, 2014, application No. is 201410620116.5, entitled " gases
The divisional application of the patent application of generator ".
Technical field
The invention relates to a kind of gas generators, in particular to a kind of protected against explosion gas generator.
Background technique
All the time, the mankind are completely to pay attention to for life, and the exploitation of the technology of many medical treatment is all for fighting disease
Disease, to continue the life of the mankind.Past medical mode be all largely belong to it is passive, that is, when disease occurs, then right
Disease carries out medical treatment, for example, operation, administration, the chemotherapy of even cancer, the maintenance of radiation treatment or chronic disease, rehabilitation,
Correction etc..But in recent years, many medical experts are increasingly towards preventative medical procedures and study, such as health food
Research, genetic disease screening and prevention etc. ahead of time, the possible morbidity of futurity that is directed to of even more active are prevented.In addition,
In order to extend human longevity, many anti-aging, oxidation resistant technologies are gradually developed, and are widely used by masses, comprising applying
Skin care products and antioxidation foodstuff/drug for smearing etc..
It has been investigated that: human body causes not because of a variety of causes, (such as disease, diet, local environment or living habit)
Stable oxygen (O+), also known as free radical (harmful free radicals), the water of part can be mixed into the hydrogen of sucking, and are excreted.Between
The quantity for reducing human free radical is connect, the alkaline constitution that acidic constitution is restored to health is reached, can be anti-oxidant, anti-aging, into
And also reaches and eliminate chronic disease and beauty and health care effect.Even there is clinical trial to show, for it is some long beds confined to bed patient,
Because breathing high concentration oxygen for a long time, caused by injury of lungs, the symptom of injury of lungs can be alleviated through sucking hydrogen.
It is heated or is burnt in addition, the purposes of oxyhydrogen in addition to above-mentioned health care, also can be used for generating oxyhydrogen flame, in addition
The purposes such as engine carbon deposit can be removed.And general oxyhydrogen is generated via electrolytic tank electrolysis liquid water, however liquid electrolyte
It is easy to generate high temperature during water, the oxyhydrogen electrolytic cell to avoid gas gas explosion traditional is mostly to utilize ventilation type, that is, make
Cooled down with fan, but if fan failure will will lead to oxyhydrogen electrolyzer temperature and increase and lead to the danger of gas explosion.
Summary of the invention
Therefore, one of viewpoint of the invention is to provide a kind of gas generator, and liquid electrolyte water simultaneously generates hydrogen-oxygen mixing
Gas, meanwhile, the amount of hydrogen and oxygen gas mixture in water tank can be kept, the temperature of hydrogen and oxygen gas mixture can also be reduced, to prevent
The generation of gas explosion.
The present invention provides a kind of gas generator, includes water tank and electrolysis unit.Water tank has one first hollow portion, should
First hollow portion is equipped with an electrolysis water.Electrolysis unit is set within the first hollow portion of water tank, to be electrolysed electrolysis water with
Generate a hydrogen and oxygen gas mixture.Wherein when electrolysis unit operates, the water level of the first hollow portion Inner electrolysis water between 90%~
Between 100% full-water level.
When electrolysis unit starts to be electrolysed electrolysis water, electrolysis water must riddle the first hollow portion of water tank and be in full water
Position, after electrolysis unit is electrolysed electrolysis water, the water level that electrolysis water fills the first hollow portion of water tank is higher than the 90% of full-water level.
Water tank further selectively have a conduit.Conduit is to export hydrogen and oxygen gas mixture.When electrolysis unit is temporary
When the solution that has a power failure electrolysis water is to generate hydrogen and oxygen gas mixture, conduit can be used to supplement input electrolysis water, so that electrolysis water is full of the
One hollow portion and electrolysis unit.
Furthermore gas generator of the invention, which obtains, selectively additionally comprises a pumping plant.The of pumping plant and water tank
One hollow portion is interconnected, and is placed in the electrolysis water in the first hollow portion to forced circulation.
Gas generator of the invention, which obtains, selectively to be additionally comprised comprising a partition.Partition includes an intercommunicating pore.Partition is used
The first hollow space is divided into a top and a lower part.Top and lower part are interconnected by intercommunicating pore.
Electrolysis unit further selectively include multiple electrodes, a backing plate and a cell body.Multiple electrodes difference
It is arranged at intervals within cell body and forms multiple electrodes runner.Backing plate is set to each electrode and has multiple upper perforation.
The top of first hollow portion and multiple electrodes runner are multiple upper perforation by backing plate to be interconnected.And each electrode runner
It is to be connected to each independently by corresponding upper perforation with the top of the first hollow portion.
Cell body further selectively have a lower surface.The lower surface of cell body has multiple lower perforation.
The lower part of first hollow portion and multiple electrodes runner are multiple lower perforation by the lower surface of cell body to be interconnected.And
Each electrode runner is to be connected to each independently by corresponding lower perforation with the lower part of the first hollow portion.
Gas generator of the invention, which obtains, selectively additionally comprises a flow rate detector.Flow rate detector coupling electrolysis dress
It sets, to detect the flow of hydrogen and oxygen gas mixture, and so as to the quantum of output of hydrogen and oxygen gas mixture in control electrolysis unit.Wherein flow
Cut off to the detector property of can choose being electrically connected for the electrolysis unit and power supply.Electrolysis unit generate hydrogen and oxygen gas mixture via
The first hollow portion of water tank and the electrolysis water of electrolysis unit are riddled, the amount of hydrogen and oxygen gas mixture in water tank can be kept, also
The temperature of hydrogen and oxygen gas mixture can be reduced, to prevent the generation of gas explosion.
Gas generator of the invention, which obtains, selectively additionally comprises a power supply.Multiple electrodes include a cathode sheets, a sun
Pole piece and multiple bipolar electrode pieces.Multiple bipolar electrode pieces are arranged at intervals between cathode sheets and anode strip.Cathode sheets
It is connected to the cathode of power supply, anode strip is connected to the anode of power supply.
Gas generator of the invention, which obtains, selectively additionally comprises one atomization/volatilization gas mixing channel.Atomization/volatilization gas
Mixing channel connects water tank, and to receive hydrogen and oxygen gas mixture, atomization/volatilization gas mixing channel generates an atomization gas and mixes with hydrogen-oxygen
Gas mixing is sucked with forming a health care gas for user, and wherein atomization gas is selected from by water vapour, is atomized liquid medicine, is waved
Send out essential oil and combinations thereof, one of composed group.
In terms of comprehensive, of the invention to focus on proposing a kind of gas generator, it includes water tank and electrolysis units.This hair
The design that bright middle electrolysis unit is set to water tank can save space, while the hydrogen and oxygen gas mixture that electrolysis unit generates is by being full of
It in the electrolysis water of the first hollow portion of water tank, can be present in water tank to avoid air cavity, the temperature of electrolysis unit can also be made to drop
It is low, to prevent the generation of gas explosion.Furthermore the gas vent of electrolysis unit and water inlet design in the present invention, so that in water tank
Electrolysis water can be supplemented to electrolysis unit, and hydrogen and oxygen gas mixture caused by electrolysis unit can be discharged water tank, reach
Air water circulation.Further, in the present invention, the interconnected structure of pumping plant, water tank and electrolysis unit is designed, and can make to hold
It is placed in electrolysis water in the first hollow portion and carries out forced circulation, so that the air cavity in water tank is leveled off to zero, to prevent the generation of gas explosion.
Detailed description of the invention
Figure 1A and Figure 1B is the signal for being painted the different perspectives of gas generator of the invention in the first specific embodiment
Figure；
Fig. 2A and Fig. 2 B is different perspectives when only having tank upper cover and electrolysis unit combination in Figure 1A illustrated embodiment
Schematic diagram；
Fig. 3 A and Fig. 3 B are different perspectives when only having electrolysis unit and the combination of water tank groove body in Figure 1A illustrated embodiment
Schematic diagram；
Fig. 4 A and Fig. 4 B are to be painted the electrolysis unit of the gas generator of the present invention different perspectives in Figure 1A illustrated embodiment
Explosive view；
Fig. 5 A and Fig. 5 B are water tank groove body and the electrolysis unit reality shown in Fig. 3 A for being painted gas generator of the invention
It applies the top view of example and cuts open the sectional view set along the line A-A of the top view；
Fig. 6 is the schematic diagram of different perspectives when only having cell body, partition and electrode combination in Figure 1A illustrated embodiment；
Fig. 7 A and Fig. 7 B are water tank groove body and the electrolysis unit reality shown in Fig. 3 A for being painted gas generator of the invention
It applies the top view of example and cuts open the sectional view set along the line B-B of the top view；
Fig. 8 is the schematic diagram for being painted gas generator of the invention in the second specific embodiment；
Fig. 9 A and Fig. 9 B are the signals for being painted the different perspectives of gas generator of the invention in the tenth specific embodiment
Figure；
Figure 10 A and Figure 10 B are different views when only having condensate filter and water tank cover assembling in Fig. 9 A illustrated embodiment
The schematic diagram at angle；
Figure 11 is the schematic diagram being painted when not having water tank lid in Figure 10 A illustrated embodiment；
Figure 12 is the schematic diagram being painted when not having filter screen in embodiment illustrated in fig. 11；
Figure 13 is the schematic diagram being painted when not having filtering square in embodiment illustrated in fig. 12；
Figure 14 A and Figure 14 B are the condensate filter embodiments shown in Figure 10 A for being painted gas generator of the invention
Top view and the sectional view set is cutd open along the line C-C of the top view；
Figure 15 A and Figure 15 B are the different perspectivess for being painted gas generator of the invention in the 14th specific embodiment
Schematic diagram；
Figure 16 is painted in Figure 15 A illustrated embodiment only with the schematic diagram of humidification device；
Figure 17 is the schematic diagram for being painted gas generator of the invention in the 5th specific embodiment；
Figure 18 A and Figure 18 B are the different perspectivess for being painted gas generator of the invention in the 15th specific embodiment
Schematic diagram；
Figure 19 is the rearview for being painted gas generator of the invention in the embodiment shown in Figure 18 A；
Figure 20 A and Figure 20 B are to be painted in Figure 18 A illustrated embodiment the only top view with condensate filter and water tank lid
And the sectional view set is cutd open along the line D-D of the top view.
About advantages of the present invention, spirit and feature will be described in detail and beg for embodiment and referring to appended attached drawing
By.
[symbol description]
W: electrolysis water W2: supplement water
G: hydrogen and oxygen gas mixture G2: atomization gas
H: hydrogen water
1: gas generator 2: water tank
20: the first hollow portions 200: top
202: lower part 22: conduit
24: water tank groove body 240: first base
242: the first wall portion, 244: the first opening portion
246: the first embedded structure, 248: the first lateral margin
249a: water outlet 249b: water inlet
26: water tank lid 260: second base
261: 262: the second wall portion of cap bore
264: the second hollow portion, 266: the second opening portion
28: gasket 280: third opening portion
282: third embedded structure 3: electrolysis unit
30: partition 300: intercommunicating pore
32: 320: the four pedestal of cell body
3202: lower perforation 3204: groove
322: fourth wall 3220: fixed column
324: the four hollow portion, 326: the four opening portion
33: electrode column 34: multiple electrodes
340: cathode sheets 342: anode strip
344: bipolar electrode piece 36: backing plate
360: above perforating 37: upper cover body
370: first runner 38: lower cover
380: second flow channel 4: atomization/volatilization gas mixing channel
5: pumping plant 50: water inlet pipe
52: outlet pipe 6: condensate filter
60: blowhole 600: filter screen
602: filtering square 62: venthole
64: condensate film 640: circulatory flow
640a: runner 642: gradual-enlargement type runner
644: connection runner 7: cooling device
70: radiator 700: cabinet
702: heat-dissipating pipe 704: entrance
706: outlet 72: fan
82: flow rate detector 9: humidification device
90: 92: the second conduit of hollow body
94: efferent duct 95: rocking equipment
96: 98: the four conduit of third conduit
Specific embodiment
In order to allow advantages of the present invention, spirit and feature can more easily and be expressly understood that, it is subsequent will be with embodiment simultaneously
It is described in detail and discusses referring to appended attached drawing.It is worth noting that, these embodiments are only the representative embodiment of the present invention,
Middle illustrated ad hoc approach, device, condition, material etc. is not intended to limit the invention or corresponding embodiment.
Firstly, the present invention proposes a kind of gas generator, it is a kind of protected against explosion gas generator.Please refer to Figure 1A, figure
1B, Fig. 2A and Fig. 2 B, Figure 1A and Figure 1B are the different perspectivess for being painted gas generator of the invention in the first specific embodiment
Schematic diagram, Fig. 2A and Fig. 2 B is the different perspectives only having when tank upper cover and electrolysis unit combine in Figure 1A illustrated embodiment
Schematic diagram, as shown, gas generator 1 of the present invention includes water tank 2 and electrolysis unit 3 in first embodiment.Water tank
2 are equipped with an electrolysis water W, and electrolysis unit 3 is set in water tank 2, to be electrolysed electrolysis water W to generate a hydrogen and oxygen gas mixture
G.Wherein, when electrolysis unit operates, the water level of the first hollow portion Inner electrolysis water of water tank between 90%~100% full-water level it
Between.In an embodiment, when electrolysis unit 3 starts to be electrolysed electrolysis water W, electrolysis water W riddle the first hollow portion of water tank 2 and
In full-water level, after electrolysis unit 3 is electrolysed electrolysis water W, the water level that electrolysis water W fills the first hollow portion of water tank 2 is higher than full
The 90% of water level.The design to each element of the invention is first illustrated respectively below.
Firstly, water tank 2 of the present invention has one first hollow portion 20 and a conduit 22.In the first of water tank 2
Empty portion 20 is adapted for accommodating an electrolysis water W.Electrolysis water W main ingredient is pure water, can optionally add a small amount of electrolyte, such as
Sodium hydroxide, calcium carbonate, sodium chloride etc..First hollow portion 20 of the conduit 22 of water tank 2 and water tank 2 be it is interconnected, to defeated
Out in the hydrogen and oxygen gas mixture G as caused by electrolysis unit 3 and supplement input electrolysis water W to water tank 2.
Further, please referring to Fig. 3 A and Fig. 3 B, Fig. 3 A and Fig. 3 B is the water tank for being painted gas generator of the invention
The explosive view of different perspectives in the specific embodiment shown in Figure 1A.In this present embodiment, water tank 2 has additionally comprised a water tank groove body 24
An and water tank lid 26.
Water tank groove body 24 is roughly divided into a first base 240 and one first wall portion 242.First wall portion 242 is from the first bottom
The inner surface of seat 240 extends outward toward its normal vector direction, and the first wall portion 242 is to enclose equipped with the first hollow portion 20, should
First hollow portion 20 is to have one first opening portion 244 relative to the other end of first base 240.Meanwhile and the first wall portion 242
The other side relative to first base 240 is that have one first lateral margin 248, and first lateral margin 248 then surrounds above-mentioned first
Opening portion 244.Further, the water tank groove body 24 of water tank 2 additionally comprises an a water outlet 249a and water inlet 249b.Yu Benshi
It applies in example, the water outlet 249a of water tank groove body 24 is the first wall portion 242 of joining water box groove body 24 relative to 3 direction of electrolysis unit
Two surfaces and water tank groove body 24 water inlet 249b be joining water box groove body 24 the first wall portion 242 relative to electrolysis fill
Set two surfaces in 3 directions.Wherein, the water outlet 249a of the water tank groove body 24 and water inlet 249b of water tank groove body 24 is by first
Hollow portion 20 is connected to.The water outlet 249a of a water tank groove body 24 and water inlet 249b is handy for a pumping plant and water tank 2
First hollow portion 20 is interconnected.
Water tank lid 26 is roughly divided into a second base 260 and one second wall portion 262.Second wall portion 262 is from the second bottom
The inner surface of seat 260 extends outward toward its normal vector direction, and the second wall portion 262 is to enclose equipped with one second hollow portion 264,
Second hollow portion 264 is to have one second opening portion 266 relative to the other end of second base 260.Water tank lid 26 must pass through
First lateral margin 248 of water tank groove body 24 is covered in the second hollow portion 264 by the second opening portion 266.Conduit 22 must be set to
In the second base 260 of water tank lid 26 and the second base 260 of joining water box lid 26 is relative to 24 direction of water tank groove body
Two surfaces, but it is not limited, in practical application, conduit 22 can also by a guide hole or other with input/output function
Replaced the element of energy.Water tank lid 26 has additionally comprised multiple cap bore (as shown in Figure 10 A), multiple cap bore joining water box lids 26
Two surfaces of the second base 260 relative to 24 direction of water tank groove body, the electrode column to electrolysis device 3 runs through and is set to
Electrolysis unit 3, or with so that detection device (such as flow rate detector, water-level gauge, safety valve) runs through and is arranged on.
Further, in this present embodiment, water tank 2 has additionally comprised a gasket 28, is to be set to water tank groove body 24
And between water tank lid 26, to make water box slot body 24 combine closely with water tank lid 26.Gasket 28 is open with a third
Portion 280.When gasket 28 is set between water tank groove body 24 and water tank lid 26, the third opening portion 280 of gasket 28 is
Multiple cap bore 261 and the second opening portion 266 are enclosed and are located therein.The corresponding surface more score of water tank groove body 24 and gasket 28
Not Ju You one first embedded structure 246 and corresponding third embedded structure 282 and the two be able to it is mutually chimeric.First is chimeric
Structure 246 is to enclose the first opening portion 244 to be located therein.Third embedded structure 282 is to enclose third opening portion 280 set on it
In.
Then, please referring to Fig. 4 A and Fig. 4 B, Fig. 4 A and Fig. 4 B is to be painted the electrolysis unit of gas generator of the present invention in figure
The explosive view of different perspectives in 1A illustrated embodiment.Electrolysis unit 3 include a cell body 32, multiple electrodes 34, backing plate 36, on
Lid 37 and lower cover 38.Plurality of electrode 34, which is respectively separated, is set within cell body 32 and is formed multiple electrodes stream
Road S1.Backing plate 36 is set to the upper surface of each electrode 34.Upper cover body 37 is covered on backing plate 36 relative to the another of cell body 32
One end.Lower cover 38 is covered on the other end of the lower surface of cell body 32 relative to upper cover body 37.
Further, Fig. 5 A and five B is please referred to, Fig. 5 A and Fig. 5 B are the water box slots for being painted gas generator of the invention
The top view of the embodiment of body and the electrolysis unit embodiment shown in Fig. 3 A and the section set is cutd open along the line A-A of the top view
Figure.Electrolysis unit separately has a partition 30.Partition 30 be from cell body relative to water tank 2 side surface toward its normal vector direction
Extend outward, the first hollow portion 20 of water tank 2 is separated into a top 200 and a lower part 202.Partition 30 includes one
Intercommunicating pore 300.Intercommunicating pore 300 is connected to two surfaces of the partition 30 relative to 240 direction of first base of water tank groove body 24.In first
The top 200 and lower part 202 in empty portion 20 are interconnected by intercommunicating pore.But the design of intercommunicating pore not to be depicted in this implementation
Limit, in practical application, the quantity or external form of intercommunicating pore all must be depending on voluntarily selecting design using upper actual demand.
Then, referring to Fig. 6, Fig. 6 is only has cell body, partition and electrode combination in Figure 1A illustrated embodiment when not
With the schematic diagram at visual angle.Cell body 32 is roughly divided into one the 4th pedestal 320 and a fourth wall 322.Fourth wall 322 is certainly
The inner surface of 4th pedestal 320 extends outward toward its normal vector direction, and fourth wall 322 be enclose it is hollow equipped with the 4th
Portion 324, the 4th hollow portion 324 are to have one the 4th opening portion 326 relative to the other end of the 4th pedestal 320.4th hollow portion
324 are suitable for accommodating electrolysis water W.In addition, being purposely to omit in Fig. 6 to express the design of cell body of the present invention
There are multiple electrodes therein, however, in practical application, must be depending on voluntarily selecting design using upper actual demand.
Then, please referring to Fig. 5 A, Fig. 5 B, Fig. 6, Fig. 7 A and Fig. 7 B, Fig. 7 A and Fig. 7 B is to be painted gas of the invention to generate
The top view of water tank groove body and the electrolysis unit embodiment shown in Fig. 3 A of device and the section set is cutd open along the line B-B of the top view
Figure.In this present embodiment, the lower surface of cell body 32 is the 4th pedestal 320 of cell body 32.The of cell body 32
Four pedestals 320 have multiple lower perforation 3202.4th pedestal 320 of multiple 3202 connection cell bodies 32 of lower perforation is relative to water
Two surfaces in 240 direction of first base of case groove body 24.4th pedestal 320 of cell body 32 separately has multiple grooves 3204.
Multiple grooves 3204 be from the 4th pedestal 320 of cell body 32 relative to the 4th opening portion 326 surface along normal vector direction
Extend inside.Each groove 3204 is spaced between lower perforation 3202 and adjacent lower perforation 3202.It is multiple recessed
Slot 3204 is obtained to place electrode 34.Meanwhile the fourth wall 322 of cell body 32 separately has multiple fixed columns 3220.It is multiple
Fixed column 3220 be extend outward toward its normal vector direction from fourth wall 322 relative to the surface of multiple lower perforation 3202 and
At.Fixed column 3220 and adjacent fixed column 3220 obtain the electrode 34 to be fixedly placed in groove 3204.When multiple electrodes 34
It is respectively separated in the groove 3204 for being set to cell body 32 and is fixed between fixed column 3220 and adjacent fixed column 3220
When, it will form multiple electrodes runner S1 within cell body 32.Wherein each electrode runner S1 obtains right by each independently
The lower perforation 3202 answered is connected to the lower part 202 of the first hollow portion 20.
Backing plate 36 has multiple upper perforation 360.Multiple upper perforation 360 are connection backing plates 36 relative to 32 direction of cell body
Two surfaces.Further, each electrode runner S1 also each independently by corresponding upper perforation 360 and first
The top 200 in empty portion 20 is connected to.
Multiple electrodes 34 include a cathode sheets 340, an anode strip 342 and multiple bipolar electrode pieces 344.It is multiple bipolar
Property electrode slice 344 is arranged at intervals between cathode sheets 340 and anode strip 342.In this present embodiment, electrolysis unit 3 additionally comprises
Two electrode columns 33, it is to individually lock anode strip 342 and cathode sheets 340 on water tank lid 26, electrolysis unit 3 is hanging
Ground is fixedly arranged in water tank 2.Further, in this present embodiment, gas generator 1 additionally comprises a power supply and (is not illustrated in figure
In).Cathode sheets 340 must be connected to the cathode of power supply, and anode strip 342 must be connected to the anode of power supply, wherein by two adjacent pairs
The voltage difference for one group of electrolysis electrode that polar electric pole piece is constituted is about between 1.5V~3V.In an embodiment, cathode sheets 340
The voltage difference of the one group of electrolysis electrode constituted with bipolar electrode piece 344 is about between 1.5V~3V.In another embodiment
In, the voltage difference for one group of electrolysis electrode that bipolar electrode piece 344 and adjacent bipolar electrode piece 344 are constituted about between
Between 1.5V~3V.In another embodiment, one group of electrolysis electrode that bipolar electrode piece 344 and anode strip 342 are constituted
Voltage difference is about between 1.5V~3V.
Upper cover body 37 includes an at least first runner 370.As shown in Figure 4 B, first runner 370 is opposite from upper cover body 37
Extend inside in the surface of backing plate 36 along normal vector direction.Multiple upper perforation 360 and the first hollow portion positioned at backing plate 36
20 are interconnected by an at least first runner 370.
Lower cover 38 includes an at least second flow channel 380.As shown in Figure 4 A, second flow channel 380 is opposite from lower cover 38
Extend inside in the surface of the 4th pedestal 320 of cell body 32 along normal vector direction.Positioned at the 4th of cell body 32 the
Multiple lower perforation 3202 of pedestal 320 with first hollow portion 20 are interconnected by an at least second flow channel 380.
It further, referring initially to Fig. 8, Fig. 8 is please to be painted gas generator of the invention in the second specific embodiment
Schematic diagram.In the second specific embodiment, gas generator 1 of the invention additionally comprise a pumping plant 5 (in Fig. 8 only with
Dotted line is painted).Pumping plant 5, which is obtained, is placed in the first hollow portion 20 and interior electrolysis water W to forced circulation.Pumping plant 5 wraps
Containing a water inlet pipe 50 and an outlet pipe 52.Water inlet of the outlet pipe 52 of pumping plant 5 to supply water pump installation 5 and the water tank 2
249b is connected with each other.The water inlet pipe 50 of pumping plant 5 is connected with each other to the water outlet 249a of supply water pump installation 5 and the water tank 2.
Further, in third specific embodiment, gas generator 1 of the invention additionally comprises one atomization/Volatile Gas
Body mixing channel 4 (as shown in fig. 15).Atomization/volatilization gas mixing channel 4 must be connected to electrolysis unit 3, to receive hydrogen-oxygen mixing
Gas G.Atomization/volatilization gas mixing channel 4 can generate an atomization gas G2 and mix with hydrogen and oxygen gas mixture G, to form a health care
Gas is sucked for the user.In practical application, atomization gas G2 must be atomized liquid medicine, volatile spirits selected from by water vapour
And combinations thereof, one of composed group.
More than, after the Separate designs to each element are illustrated, below by each element to a kind of gas generator
Combination and its application be described.
In the electrolysis unit 3 being completed, multiple electrodes 34, which are respectively separated, is set to cell body 32, and backing plate 36 is arranged
In the upper surface of each electrode 34, upper cover body 37 is covered on the other end of the backing plate 36 relative to cell body 32, and lower cover 38 covers
The other end set on the lower surface of cell body 32 relative to upper cover body 37.
In the water tank 2 and electrolysis unit 3 being completed, group install after electrolysis unit 3 anode strip 342 and cathode sheets
340 are locked on water tank lid 26 separately by two electrode columns 33.And detection device (such as flow rate detector 82) by through
Multiple cap bore 261 of water tank lid 26 are simultaneously set on water tank lid 26.Gasket 28 is arranged at water tank groove body 24, and passes through
The third embedded structure 282 of gasket 28 and the first embedded structure 246 of water tank groove body 24 are mutually chimeric.The of water tank groove body 24
One lateral margin 248 is covered in the second hollow portion 264 of water tank lid 26 by the second opening portion 266 of water tank lid 26, with
Water tank groove body 24 and water tank lid 26 are combined closely, and electrolysis unit 3 is vacantly fixedly arranged in water tank 2.Wherein, water tank 2
It is interconnected with electrolysis unit 3.
Then, in the water tank 2, electrolysis unit 3 and pumping plant 5 being completed, water tank 2 is to pass through with pumping plant 5
The connection of water inlet 249a of the outlet pipe 52 and water tank 5 of pumping plant 5 and the water inlet pipe 50 of pumping plant 5 and water tank 5
The connection of water outlet 249a is to be interconnected.Further, in 3rd embodiment, atomization/volatilization gas mixing channel 4 is to connect
Connect electrolysis unit 3.
In practical application, water tank 2 is equipped with an electrolysis water W, and electrolysis unit 3 is set in water tank 2, to be electrolysed the electricity
Water W is solved to generate a hydrogen and oxygen gas mixture G.The hydrogen and oxygen gas mixture G of electrode runner S1 is resulted from via corresponding backing plate 36
Upper perforation 360 and the first runner 370 of corresponding upper cover body 37 be input to the first hollow portion 20.It is hollow to be input to first
The hydrogen and oxygen gas mixture G in portion 20 further via water tank 2 conduit 22 export, and for user suck, but not as
Limit, in practical application, the hydrogen and oxygen gas mixture G for being input to the first hollow portion 20 can be further and via atomization/Volatile Gas
The atomization gas G2 mixing that body mixing channel 4 generates, is sucked with forming health care gas for user.
In addition, conduit 22 can be used to mend when electrolysis unit 3 suspends electrolysis electrolysis water W to generate hydrogen and oxygen gas mixture G
Input electrolysis water W is filled, so that electrolysis water W is full of the first hollow portion 20 and/or electrolysis unit 3.Supplement the first hollow portion 20 of input
Electrolysis water W via electrolysis unit 3 lower cover 38 second flow channel 380 and multiple lower perforation 3202 be input to it is corresponding
Electrode runner S1, to provide required electrolysis water W when electrolysis unit 3 is electrolysed.Wherein, when electrolysis unit operates, in first
The water level of empty portion's Inner electrolysis water is between 90%~100% full-water level.Full-water level refers to that electrolysis water is full of in one embodiment
First hollow portion of water tank.In an embodiment, when electrolysis unit 3 starts to be electrolysed electrolysis water W, electrolysis water W is filled in water
First hollow portion of case 2 and be in full-water level, when electrolysis unit 3 be electrolysed electrolysis water W after, electrolysis water W fill water tank 2 first in
The water level in empty portion is higher than the 90% of full-water level.In an embodiment, gas generator of the present invention must be detected by water-level gauge and be accommodated
Water level in the first hollow portion and/or electrolysis unit of water tank whether supplement to control electrolysis water, makes electrolysis water fill water
The water level of first hollow portion of case is higher than the 90% of full-water level.Therefore the design of gas generator of the present invention is avoided that air cavity exists
In in water tank, more the temperature of electrolysis unit can reduce, to reduce the risk of high temperature gas explosion and improve its safety.
In addition, the first hollow portion 20 of water tank 2 is further interconnected with pumping plant 5.Pumping plant 5 can be to
Forced circulation is placed in the electrolysis water W in the first hollow portion 20.Positioned at the top 200 of the first hollow portion 20 and the electricity of lower part 202
Xie Shui is recycled via intercommunicating pore 300.Wherein, after electrolysis unit is electrolysed electrolysis water W, electrolysis water W fills the of water tank 2
The water level of one hollow portion 20 is higher than the 90% of full-water level.Further, the design of gas generator of the present invention can pass through pressure
The electrolysis water that is placed in the first hollow portion is recycled, so that the air cavity in water tank is leveled off to zero, to avoid the pressure of oxyhydrogen in water tank
Power or storage capacity, cause gas explosion.
In addition, flow rate detector 82 couples electrolysis unit 3, to detect the flow of hydrogen and oxygen gas mixture G, and so as to control electricity
Solve the quantum of output of hydrogen and oxygen gas mixture G in device 3.Wherein cut off to 82 property of can choose of flow rate detector electrolysis unit 3 and electricity
The electrical connection in source (not being illustrated in figure).
In conclusion the design that electrolysis unit is set to water tank in the present invention can save space, while electrolysis unit generates
Hydrogen and oxygen gas mixture by riddling the electrolysis water of the first hollow portion of water tank, can be present in water tank to avoid air cavity, also
Can make the temperature of electrolysis unit reduces, to prevent the generation of gas explosion.Furthermore the present invention in electrolysis unit gas vent with
Water inlet design allows the electrolysis water in water tank to be supplemented to electrolysis unit, and hydrogen and oxygen mixture caused by electrolysis unit
Body can be discharged water tank, reach air water circulation.Further, in the present invention, pumping plant, water tank and electrolysis unit are mutual
The structure of connection designs, and the electrolysis water being placed in the first hollow portion can be made to carry out forced circulation, approach the air cavity in water tank
In zero, to prevent the generation of gas explosion.
Please refer to Figure 17.In the 4th specific embodiment, the present invention separately proposes a kind of gas generator, has for one kind
The gas generator for the effect of regulation is electrolysed coolant-temperature gage and cools down the electrolysis water after generating hydrogen and oxygen gas mixture.In this implementation,
Gas generator 1 includes an electrolysis unit (not being illustrated in figure), pumping plant 5 and a cooling device 7.Electrolysis unit 3 holds
It is equipped with an electrolysis water W.Electrolysis unit 3 generates a hydrogen and oxygen gas mixture G to be electrolysed electrolysis water W.Cooling device 7 is connected to electricity
Device 3 is solved, to the electrolysis water W after cooling generation hydrogen and oxygen gas mixture G.Pumping plant 5 is connected to cooling device 7 and electrolysis fills
It sets between 3, to forced circulation electrolysis water W.
Figure 17 is please referred to, Figure 17 is the schematic diagram for being painted gas generator of the invention in the 5th specific embodiment.In
In 5th specific embodiment, gas generator 1 of the invention additionally comprises a water tank 2.Water tank 2 has one first hollow portion 20 and leads
Pipe 22 (is only represented by dotted lines) in Figure 17.First hollow portion 20 of water tank 2 is equipped with electrolysis water W.Electrolysis unit 3 is to be set to
Within first hollow portion 20 of water tank 2, the first hollow portion 20 and electrolysis unit 3 are interconnected.But not limited to this, in another
In embodiment (as shown in Fig. 3 B, Fig. 5 B and Fig. 8), gas generator 1 of the invention additionally comprises a partition 30.Partition 30 includes one
Intercommunicating pore 300.Partition 30 is to be separated into a top 200 and a lower part 202 for the first hollow portion 20.Water tank 2 separately has one to go out
A mouth of a river 249a and water inlet 249b.Top 200 and lower part 202 pass through intercommunicating pore to be interconnected.In this example, water mercury device
5 between water outlet 249a and water inlet 249b.Wherein the water outlet 249a of water tank 2 is located at the top of the first hollow portion 20
200, the water inlet 249b of water tank 2 are located at the lower part 202 of the first hollow portion 10, the electrolysis being placed in top 200 and lower part 202
Water must be by water mercury device 5 to carry out forced circulation.In different embodiments, partition 30 can be a part of electrolysis unit 3
It (as shown in fig. 4 a and fig. 4b), can also be a part of water tank 2.
Further, in the 6th specific embodiment, gas generator 1 of the invention additionally comprises one atomization/Volatile Gas
Body mixing channel 4 (as shown in fig. 15).It is mixed that atomization/volatilization gas mixing channel 4 can generate atomization gas G2 and hydrogen and oxygen gas mixture G
It closes, is sucked with forming health care gas for the user.
The design to each element of the invention is first illustrated respectively below.
Firstly, since the design of water tank 2, electrolysis unit 3, pumping plant 5 and atomization/volatilization gas mixing channel 4 structure is
In explanation made above, therefore do not repeat again herein.
Please refer to Figure 15 A, Figure 15 B and Figure 17.In fourth embodiment, cooling device 7 of the invention includes a radiator
70 and a fan 72.Radiator 70 includes a cabinet 700 and a heat-dissipating pipe 702.Heat-dissipating pipe 702 is distributed across the case of radiator 70
Within body 700.The shape of heat-dissipating pipe 702 is a coiled pipe (not being illustrated in figure), to increase integral heat sink area and then mention
High cooling efficiency, but be not limited with this shape, it can also be a spiral coil in practical application.In addition, in practical application
When, heat-dissipating pipe 702 is obtained as made by one of silver, aluminium, iron, copper, silver alloy, aluminium alloy, ferroalloy, the above material of copper alloy.More
Further, radiator 70 includes an entrance 704 and an outlet 706.The entrance 704 of radiator 70 is to be connected to the radiator 70
Cabinet 700 is the case for being connected to the radiator 70 relative to two surfaces in 702 direction of heat-dissipating pipe and the outlet 706 of radiator 70
Two surfaces of the body 700 relative to 702 direction of heat-dissipating pipe.Wherein, the entrance 704 of radiator 70 and outlet 706 are to pass through heat-dissipating pipe
702 to be interconnected.
Further, in fourth embodiment, gas generator 1 of the invention additionally comprises a microcomputer controller (not
It is illustrated in figure).Microcomputer controller is the temperature to sense electrolysis water W, and according to the temperature of the electrolysis water W sensed with
Control the flow velocity that pumping plant 5 is extracted and inputted.In addition, microcomputer controller includes that a temperature-sensitive sticker (is not illustrated in figure
In).Temperature-sensitive sticker is the temperature to sense the electrolysis water W being placed in electrolysis unit 3.In addition, microcomputer controller is another
Include a flow rate detector 82.Flow of the flow rate detector 82 to detect hydrogen and oxygen gas mixture G, and so as to controlling electrolysis unit
The quantum of output of hydrogen and oxygen gas mixture G in 3.Cut off to 82 property of can choose of flow rate detector being electrically connected for electrolysis unit 3 and the power supply
It connects and (is not illustrated in figure).
More than, after the Separate designs to each element are illustrated, below by each element combination and its
Using being described.
In the water tank 2 and electrolysis unit 3 being completed, the of water tank 2 is set to for the electrolysis unit 3 after installing group
In one hollow portion 20, wherein the first hollow portion 20 of water tank 2 and electrolysis unit 3 are interconnected.In addition, due to being completed
The combination of water tank 2 and electrolysis unit 3 does not repeat again herein in explanation made above.
Among water tank 2, electrolysis unit 3, pumping plant 5 and the cooling device 7 being completed, 2 first hollow portion of water tank
20 and electrolysis unit 3 are interconnected (not being illustrated in figure), and cooling device 7 is to be connected to water tank 2, and pumping plant 5 is connection
Between radiator 7 and water tank 2, but not limited to this, and in practical application, radiator 70 must be directly connected in electrolysis unit 3,
Pumping plant 5 must be directly connected between radiator 7 and water tank 2, imply that gas generator of the invention does not need water tank 2, or
Person, which is not required to for electrolysis unit 3 being set in water tank 2, can also complete gas generator of the invention.
Then, the above-mentioned water tank 2 being completed, electrolysis unit 3, pumping plant 5 and cooling dress are further described
Set the connection relationship between 7.Please refer to Figure 15 A and Figure 15 B.Be provided with the water tank 2 of electrolysis unit 3 water outlet 249a be with it is cold
But the entrance 704 of the radiator 70 of device 7 is connected with each other, and the outlet 706 of the radiator 70 of cooling device 7 is and pumping plant 5
Water inlet pipe 50 be connected with each other, the outlet pipe 52 of pumping plant 5 be and the water inlet 249b of water tank 2 be connected with each other.But more than not
The connection relationship stated is limited, and in practical application, the water outlet 249a for being provided with the water tank 2 of electrolysis unit 3 is obtained and pumping plant 5
Water inlet pipe 50 be connected with each other, the outlet pipe 52 of pumping plant 5 and 704 phase of entrance of the radiator 70 of cooling device 7 interconnect
It connects, the outlet 706 of the radiator 70 of cooling device 7 is obtained to be connected with each other with the water inlet 249b of water tank 2.
In practical application, water tank 2 is equipped with an electrolysis water W, and electrolysis unit 3 is set in water tank 2, to be electrolysed electrolysis
Water W is to generate a hydrogen and oxygen gas mixture G.The hydrogen and oxygen gas mixture G of electrode runner S1 is resulted from via corresponding backing plate 36
The first runner 370 of upper perforation 360 and corresponding upper cover body 37 is input to the first hollow portion 20.It is input to the first hollow portion
20 hydrogen and oxygen gas mixture G is further exported via the conduit 22 of water tank 2, and is obtained and sucked for user, and but not limited to this,
In practical application, the hydrogen and oxygen gas mixture G exported by the first hollow portion 20 can be mixed further with via atomization/volatilization gas
The atomization gas G2 mixing that slot 4 generates is closed, is sucked with forming health care gas for user.
In addition, conduit 22 can be used to mend when electrolysis unit 3 suspends electrolysis electrolysis water W to generate hydrogen and oxygen gas mixture G
Input electrolysis water W is filled, so that electrolysis water W is full of the first hollow portion 20 and/or electrolysis unit 3.Supplement the first hollow portion 20 of input
Electrolysis water W via electrolysis unit 3 lower cover 38 second flow channel 380 and multiple lower perforation 3202 be input to it is corresponding
Electrode runner S1, to provide required electrolysis water W when electrolysis unit 3 is electrolysed.
In addition, water tank 2, electrolysis unit 3, pumping plant 5 and cooling device 7 are interconnected.In in application, generating hydrogen-oxygen
Electrolysis water W after mixed gas G must force output dissipating to cooling device 7 from the water outlet 249a of water tank 2 by pumping plant 5
The entrance 704 of hot device 70, and cooled down in the heat-dissipating pipe of radiator 70 702.Electrolysis water W after cooling must be filled by water pump
Set 5 forces output to the water inlet pipe 50 of pumping plant 5 via the outlet 706 of radiator 70, and further, electrolysis water W must be logical
It crosses pumping plant 5 and forces the water inlet 249b for being input to water tank 2 via the outlet pipe 52 of pumping plant 5.Therefore, gas of the invention
Body generator can be by the electrolysis water after the cooling generation hydrogen and oxygen gas mixture of cooling device, and sets circulation by force by pumping plant
The electrolysis water, the effect of to reach heat dissipation.Wherein, the temperature for the electrolysis water being placed in the electrolysis unit is a conventional electrolysis
Temperature, in practical application, the temperature for being placed in the electrolysis water W in electrolysis unit 3 obtain between 55 DEG C~65 DEG C.
Further, microcomputer controller 8 is coupled to temperature of the pumping plant 5 to sense electrolysis water W, and according to
The temperature of the electrolysis water W sensed is to control the flow velocity that pumping plant 5 is extracted and inputted.In practical application, when via temperature
The temperature for the electrolysis water W that sensor 80 senses is higher than a preset temperature, and the excessively high information of this temperature can be communicated back to micro computer controlled
Device 8 processed, then microcomputer controller 8 further can make electrolysis water with the flow velocity for accelerating electrolysis water W to recycle by control pumping plant 5
Temperature reduce to return in preset temperature.On the contrary, when the temperature of the electrolysis water W sensed via temperature-sensitive sticker 80 is lower than one
Preset temperature, the too low information of this temperature can be communicated back to microcomputer controller 8, then microcomputer controller 8 can be controlled further
Pumping plant 5 processed increases the temperature of electrolysis water to return in preset temperature to slow down the flow velocity that electrolysis water W is recycled.It is wherein pre-
If temperature is that can provide the temperature of best electrolytic efficiency.In this present embodiment, preset temperature is a conventional electrolysis temperature.In practice
On, conventional electrolysis temperature is between 55 DEG C~65 DEG C.
In terms of comprehensive, of the invention to focus on proposing a kind of gas generator, it includes electrolysis unit, cooling device with
And pumping plant.Gas generator of the invention can generate the electrolysis water after hydrogen and oxygen gas mixture by cooling device cooling,
And cyclic electrolysis water is set by force by pumping plant, the effect of to reach heat dissipation.Meanwhile the present invention can make electrolysis water temperature be located at one
Within the temperature range of best electrolytic efficiency is provided, hydrogen and oxygen gas mixture is generated to solve energy consumption to be effectively electrolysed electrolysis water
Problem.
In addition, water tank 2, electrolysis unit 3, pumping plant 5 and radiator 70 are interconnected in an embodiment.First
Hollow portion 20 is divided into a top 200 and a lower part 202 by partition 30.After in application, generating hydrogen and oxygen gas mixture G
Electrolysis water W must force output entering to radiator 70 from the water outlet 249a on the top 200 for being located at water tank 2 by pumping plant 5
Mouth 704, and cooled down in radiator 70.Electrolysis water W after cooling must be by pumping plant 5 via the outlet of radiator 70
706 force output to the water inlet pipe 50 of pumping plant 5, and further, electrolysis water W must be filled by pumping plant 5 via water pump
The pressure of outlet pipe 52 for setting 5 is input to the water inlet 249b positioned at 2 lower part 202 of water tank.Therefore, gas generator energy of the invention
Enough by the electrolysis water after the cooling generation hydrogen and oxygen gas mixture of radiator, and circulation is set by force by pumping plant and is placed in water tank
The top of first hollow portion and the electrolysis water in lower part, the effect of to reach heat dissipation.
Please refer to Fig. 9 A and Fig. 9 B.The present invention separately proposes a kind of gas generator, is a kind of gas with filtering function
Body generator.In the 7th specific embodiment, gas generator 1 includes an electrolysis unit 3 and a condensate filter 6.Electrolysis
Device 3 accommodates an electrolysis water W (not being illustrated in figure).Electrolysis unit 3 is to be electrolysed electrolysis water W to generate a hydrogen and oxygen gas mixture
G.Condensate filter 6 connects electrolysis unit 3, one miscellaneous in hydrogen and oxygen gas mixture G to condense hydrogen and oxygen gas mixture G and filter
Matter.Condensate filter 6 can be used to input supplement water W2 (not being illustrated in figure) to electrolysis unit 3.In an embodiment, work as electricity
When solving the pause electrolysis of device 3 electrolysis water W to generate hydrogen and oxygen gas mixture G, condensate filter 6 can be used to input supplement water W2,
Impurity can be backwashed via condensate filter 6 to electrolysis unit 3 by supplement water W2.
Further, in the 8th specific embodiment, gas generator 1 of the invention additionally comprises a water tank 2.Water tank 2
With one first hollow portion 20.First hollow portion 20 of water tank 2 is equipped with electrolysis water W.Electrolysis unit 3 is set to water tank 2
Within first hollow portion 20.
Further, in the 9th specific embodiment, gas generator 1 of the invention additionally comprises one atomization/Volatile Gas
Body mixing channel 4 (as shown in fig. 15).Atomization/volatilization gas mixing channel 4 is obtained and is connect with condensate filter 6, after receiving filtering
Hydrogen and oxygen gas mixture G.It is mixed that atomization/volatilization gas mixing channel 4 can generate atomization gas G2 and filtered hydrogen and oxygen gas mixture G
It closes, is sucked with forming health care gas for the user.
Please referring to Fig. 9 A and Fig. 9 B, Fig. 9 A and Fig. 9 B is to be painted gas generator of the invention in the tenth specific embodiment
Different perspectives schematic diagram.In the tenth specific embodiment, gas generator 1 of the invention must additionally comprise a pumping plant 5
And cooling device 7.
The design to each element of the invention is first illustrated respectively below.
Firstly, since the design of water tank 2, electrolysis unit 3 and atomization/volatilization gas mixing channel 4 structure is in made above
Illustrate, therefore does not repeat again herein.
Please refer to Figure 10 A, Figure 10 B, Figure 11, Figure 12, Figure 13, Figure 14 A and Figure 14 B.Condensate filter 6 of the invention has
There are a blowhole 60 and a venthole 62.Blowhole 60 must be connected to electrolysis unit 3, to receive hydrogen and oxygen gas mixture.Out
Stomata 62 is to be discharged filtered hydrogen and oxygen gas mixture G.In addition, condensate filter 6 of the invention includes multiple condensate films
64.Each condensate film 64 has a runner 640a, the runner 640a phase of the runner 640a of condensate film 64 and adjacent condensate film 64
It is intercommunicated, so as to forming the circulatory flow 640 to circulate for hydrogen and oxygen gas mixture G, to condense hydrogen and oxygen gas mixture G.Enter gas
Hole 60 and venthole 62 are obtained to be interconnected by circulatory flow 640.In an embodiment, the runner 640a of condensate film 64 is one gradually
Expansion formula runner 642 is connected to runner 644 with one and is formed.As shown in Figure 14B, gradual-enlargement type runner 642 is the runner of a section flaring,
But be not limited with gradual-enlargement type runner 642 shown in Figure 14 B, in practical application, the cross section of gradual-enlargement type runner must in it is semi-circular,
Triangular form is trapezoidal.Gradual-enlargement type runner 642 has relatively wide one end and relatively narrow one end.Gradual-enlargement type runner 642 it is opposite
Wide one end and relatively narrow one end all have an opening.Being connected to runner 644 has a runner and two corresponding openings.Even
Two of passage flow duct 644 are corresponding to be open to be interconnected by runner.When gradual-enlargement type runner 642 be connected to 644 phase of runner
When connecting, gradual-enlargement type runner 642 be connected to opening and company of the runner 644 by relatively wide one end of gradual-enlargement type runner 642
The connection of the opening of passage flow duct 644 is interconnected.The structure of the runner 640a of condensate film 64 designs, and makes horizontal run
(i.e. gradual-enlargement type runner 642) is interconnected with vertical run (being connected to runner 644), but horizontal run is not with section flaring
Runner be limited, in practical application, horizontal run can also be the equal runner in section.Further, when condensate film 64
Runner 640a and the runner 640a of adjacent condensate film 64 when being connected with each other, the runner 640a of condensate film 64 and adjacent condensate film 64
The runner 640a opening and the connection of adjacent condensate film 64 that pass through relatively narrow one end of the gradual-enlargement type runner 642 of condensate film 64
The connection of the opening of runner 644 is interconnected.Therefore, the structure design of the runner 640a of condensate film 64, to condense
The runner 640a of piece 64 and the runner 640a of adjacent condensate film 64 are interconnected, and are circulated so as to being formed for hydrogen and oxygen gas mixture
Circulatory flow 640.It implies that in this present embodiment, the connection type of condensate film and adjacent condensate film can drive hydrogen and oxygen mixture
Body reaches more preferably condensation and filter effect by longer condensation and filtration path.Further, in an embodiment
In, it must be provided with an activated carbon fiber in runner 640a, to filter the impurity in hydrogen and oxygen gas mixture G.Runner 640a is obtained separately
It is provided with any filtering material as composed by ceramics, quartz, diatomite, sepiolite or combination of the above, filtering material can be more
Further filter the impurity in hydrogen and oxygen gas mixture G.Wherein impurity is the electrolyte in electrolysis water W, is sodium hydroxide.But
It is not limited, in practical application, impurity must be calcium carbonate, sodium chloride etc..In addition, of the invention enters in an embodiment
Stomata 60 is obtained to be made of a filter screen 600 and a filtering square 602.Filter screen 600 and filtering square 602 must be connected to electrolysis
Device 3 to receive hydrogen and oxygen gas mixture G, and preliminarily filters hydrogen and oxygen gas mixture G.Wherein electrolysis unit 3 is to be placed in water
Case 2 with condensate filter 6 further to connect.
More than, after the Separate designs to each element are illustrated, below by each element combination and its
Using being described.
In the electrolysis unit 3 being completed, multiple electrodes 34, which are respectively separated, is set to cell body 32, and backing plate 36 is arranged
In the upper surface of each electrode 34, upper cover body 37 is covered on the other end of the backing plate 36 relative to cell body 32, and lower cover 38 covers
The other end set on the lower surface of cell body 32 relative to upper cover body 37.
In the water tank 2 and electrolysis unit 3 being completed, group install after electrolysis unit 3 anode strip 342 and cathode sheets
340 are locked on water tank lid 26 separately by two electrode columns 33.And detection device (such as flow rate detector 82) by through
Multiple cap bore 261 of water tank lid 26 are simultaneously set on water tank lid 26.Gasket 28 is arranged at water tank groove body 24, and passes through
The third embedded structure 282 of gasket 28 and the first embedded structure 246 of water tank groove body 24 are mutually chimeric.The of water tank groove body 24
One lateral margin 248 is covered in the second hollow portion 264 of water tank lid 26 by the second opening portion 266 of water tank lid 26, with
Water tank groove body 24 and water tank lid 26 are combined closely, and electrolysis unit 3 is vacantly fixedly arranged in water tank 2.Wherein, water tank 2
It is interconnected with electrolysis unit 3.
In the water tank 2, electrolysis unit 3 and condensate filter 6 being completed, be provided with the water tank 2 of electrolysis unit 3 with it is cold
Solidifying filter 6 is by the connection between the conduit 22 of water tank 2 and the blowhole 60 of condensate filter 6 to be interconnected.More into
One step, atomization/volatilization gas mixing channel 4 must be connected to the venthole 62 of condensate filter 6.
In practical application, water tank 2 is equipped with an electrolysis water W, and electrolysis unit 3 is set in water tank 2, to be electrolysed electrolysis
Water W is to generate a hydrogen and oxygen gas mixture G.The hydrogen and oxygen gas mixture G of electrode runner S1 is resulted from via corresponding backing plate 36
The first runner 370 of upper perforation 360 and corresponding upper cover body 37 is input to the first hollow portion 20.It is input to the first hollow portion
20 hydrogen and oxygen gas mixture G is further exported via the conduit 22 of water tank 2.The hydrogen-oxygen mixing exported by the conduit 22 of water tank 2
Gas G, which is obtained, to be condensed and is filtered into condensate filter 6 via the blowhole 60 of condensate filter 6.Into condensate filter 6
Blowhole 60 hydrogen and oxygen gas mixture G can first pass through first filter screen 600 and filtering square 602 preliminarily filtered.It connects
, carrying out preliminarily filtered hydrogen and oxygen gas mixture G can be condensed further into circulatory flow 640, meanwhile, hydrogen-oxygen
Mixed gas G must be filtered by the activated carbon fiber and filtering material being set in runner 640a and can be adsorbed in impurity
In 640 in circulatory flow.Then, filtered hydrogen and oxygen gas mixture G must be exported by the venthole 62 of condensate filter 6 and be filtered
Hydrogen and oxygen gas mixture G afterwards, and obtain and sucked for user, but not limited to this, in practical application, defeated by condensate filter 6
Filtered hydrogen and oxygen gas mixture G out can be further and via atomization/generation of volatilization gas mixing channel 4 atomization gas G2
Mixing is sucked with forming health care gas for user.
In addition, in an embodiment, it is cold when electrolysis unit 3 suspends electrolysis electrolysis water W to generate hydrogen and oxygen gas mixture G
The venthole 62 of solidifying filter 6 can be used to input to supplement water W2.The benefit supplemented by the venthole 62 of condensate filter 6
Water-filling W2 is obtained and is input in the first hollow portion 20 of water tank 2 via the conduit 22 connecting with venthole 62.In supplement input first
The electrolysis water W in empty portion 20 is obtained to be input to via the second flow channel 380 and multiple lower perforation 3202 of the lower cover 38 of electrolysis unit 3
Corresponding electrode runner S1, to provide electrolysis water W required when electrolysis unit 3 is electrolysed.And it is adsorbed in following for condensate filter 6
Impurity in circulation road 640 can also be backwashed via blowhole 60 and conduit 22 to being provided with electrolysis by above-mentioned supplement water W2
In the water tank 2 of device 3.
In addition, the flow rate detector 82 of coupling electrolysis unit 3 can detect the stream of hydrogen and oxygen gas mixture G in an embodiment
Amount.Wherein, the generation flow rate of the hydrogen and oxygen gas mixture G of gas generator 1 is between 0.01L/min. and 12L/min..
In terms of comprehensive, of the invention to focus on proposing a kind of gas generator, it includes electrolysis unit and condensed
Filter.In gas generator of the invention, hydrogen and oxygen gas mixture caused by electrolysis unit can by condensate filter into
Row condenses and filters impurity therein, to provide the hydrogen and oxygen gas mixture of a suitable human body sucking.Meanwhile setting through the invention
Meter can backwash electrolyte to electrolysis unit while supplementing water, to reduce the consumption of electrolyte and avoid electrolyte
Block in condensate filter.
Please refer to Figure 15 A, Figure 15 B and Figure 16.In the 11st specific embodiment, the present invention separately proposes that a kind of gas generates
Device is a kind of gas generator for having humidification function.Gas generator 1 include an electrolysis unit 3 (not being illustrated in figure) and
One humidification device 9.Electrolysis unit 3 is equipped with electrolysis water W, to be electrolysed electrolysis water W to generate a hydrogen and oxygen gas mixture G.Humidifying
Device 9 connects electrolysis unit 3, to receive simultaneously humidifying hydrogen and oxygen gas mixture G.
Further, in the 12nd specific embodiment, gas generator 1 of the invention additionally comprises a condensate filter
6.Condensate filter 6, which obtains, to be set between electrolysis unit 3 and humidification device 9, to condense the mixing of hydrogen-oxygen caused by electrolysis unit 3
Gas G simultaneously filters the impurity in hydrogen and oxygen gas mixture G.Humidification device 9 is to receive the simultaneously filtered hydrogen and oxygen mixture of humidifying
Body.
Further, in the 13rd specific embodiment, gas generator 1 of the invention additionally comprises one atomization/volatilization
Gas mixing tank 4.Atomization/volatilization gas mixing channel 4 must be connected to the humidification device connecting with condensate filter, to receive
Hydrogen and oxygen gas mixture G after filter and humidifying.After atomization/volatilization gas mixing channel 4 can generate atomization gas G2 and filtering and humidifying
Hydrogen and oxygen gas mixture G mixing, with formed health care gas for user suck.But not limited to this, in another embodiment, mist
Change/volatilization gas mixing channel 4 must be connected to humidification device, to receive the hydrogen and oxygen gas mixture G after humidifying.Atomization/Volatile Gas
Body mixing channel 4 can generate atomization gas G2 and mix with the hydrogen and oxygen gas mixture G after humidifying, be inhaled with forming health care gas for user
Enter.But not limited to this, and in an embodiment, it is a hand-held atomising device that atomization of the invention/volatilization gas mixing channel 4, which obtains,
(not being illustrated in figure).Hand-hold atomization device must connect humidification device 9, to receive the hydrogen and oxygen gas mixture after humidifying.Hand
It holds formula atomising device one atomization gas of generation to mix with the hydrogen and oxygen gas mixture after humidifying, be inhaled with forming health care gas for user
Enter.But not limited to this, and in another embodiment, hand-hold atomization device must connect the humidifying dress connecting with condensate filter
It sets, to receive the hydrogen and oxygen gas mixture after filtering and humidifying.Hand-hold atomization device generates atomization gas and filtering and humidifying
Hydrogen and oxygen gas mixture mixing afterwards, is sucked with forming health care gas for user.In practical application, hand-hold atomization device is
With a push type structure, user can export health care gas through the push type structure of pressing hand-hold atomization device
Aequum sucks.Wherein atomization gas must be selected from the race as composed by water vapour, atomization liquid medicine, volatile spirits and combinations thereof
One of group.
Please referring to Figure 15 A and Figure 15 B, Figure 15 A and Figure 15 B is to be painted gas generator of the invention in the 14th specific reality
Apply the schematic diagram of the different perspectives in example.Further, in the 14th specific embodiment, gas generator 1 of the invention
Additionally comprise water tank 2, water mercury device 5, cooling device 7, a gas output device 10.Wherein gas output device 10 is obtained to export
Health care gas is sucked for user, and health care gas is the mixing of the hydrogen and oxygen gas mixture G and atomization gas G2 after humidifying.
The design to each element of the invention is first illustrated respectively below.
Firstly, since condensate filter 6 and the design of atomization/volatilization gas mixing channel 4 structure be in explanation made above,
Therefore it does not repeat again herein.
Humidification device 9 of the invention includes a hollow body 90, one second conduit 92, the shake of an at least efferent duct 94, one
Swing device 95 (being only represented by dotted lines in Figure 15 B), a third conduit 96 and one the 4th conduit 98.Hollow body 90 to
One supplement water W2 of accommodating.Second conduit 92, which is set to obtain on hollow body 90, (is not illustrated in figure to connect with electrolysis unit 3
In).An at least efferent duct 94 is set among hollow body 90 and connect with the second conduit 92.Second conduit 92 is and two export
Pipe 94 is connected to form a T-type structure, and but not limited to this, in practical application, the second conduit must be adjusted depending on service condition
With the connection between an at least efferent duct 94.Further, the surface of two efferent ducts 94 all has multiple perforation.Implement in one
In example, nanoscale aperture of perforating to have is in the range of 2 nanometers to 10 nanometers, to be refined gas with shape
At diffluent bubble disintegration, but not limited to this, and in practical application, the pore size of perforation must regard the progress of user's demand
Adjustment.The end for connecting two efferent ducts 94 of the second conduit 92 is all respectively arranged with a rubber stopper, to make by the second conduit 92
Received hydrogen and oxygen gas mixture G be expelled to hollow body by multiple nanometers of perforation (not being illustrated in figure) of two efferent ducts 94
90, but not limited to this, and in practical application, the end for connecting two efferent ducts 94 of the second conduit 92 can also set to be closed
Meter.In an embodiment, rocking equipment 95 must be set to the lower section among hollow body 90 and being located at an at least efferent duct 94, use
Water is supplemented with concussion.It includes a sonicator that rocking equipment 95, which obtains, for shaking to the supplement water in hollow body 90
It swings.In practice, rocking equipment is not limited only to the sonicator of this specific embodiment, and position is also not limited to Figure 15 B
Shown in position, it is any be set on hollow body and water can be shaken or stir with effectively disperse hydrogen and oxygen gas mixture at
The device of micro-bubble belongs to rocking equipment defined in the present invention.For example, rocking equipment 95 also may include centrifuge blade with
And the drive motor of connection centrifuge blade, drive motor can drive centrifuge blade to rotate and generate vortex with Yu Shuizhong, assist hydrogen-oxygen
Hydrogen in mixed gas is more effectively dispersed in water and forms hydrogen water.Rocking equipment 95 also may include above-mentioned ultrasonic
Oscillator, centrifuge blade and drive motor enable the generation of hydrogen water more efficiently.Third conduit 96 must be set to hollow body 90
On, to export hydrogen water H or to supplement input supplement water W2.In practical application, third conduit must be connected to a guide hole,
Hydrogen water H is poured out by guide hole by third conduit or pours into supplement water W2.4th conduit 98 must be set to hollow body 90
On, to export the hydrogen and oxygen gas mixture G after humidifying.
Further, in another example, gas generator 1 of the invention additionally comprises a water tank 2.Water tank 2 has one the
One hollow portion 20.First hollow portion 20 of water tank 2 is equipped with electrolysis water W.Electrolysis unit 3 is be set to water tank 2 first hollow
Within portion 20.In addition, humidification device 9 of the invention must additionally comprise one second water mercury device (not being illustrated in figure).Second water mercury
Device must be set on water tank lid 26 and be connected to the first hollow portion 20, to extract the gas inside water tank 2 so that in it
Portion generates a negative pressure.
More than, after the Separate designs to each element are illustrated, below by each element combination and its
Using being described.
In the electrolysis unit 3 that one is completed, multiple electrodes 34, which are respectively separated, is set to cell body 32, and backing plate 36 is arranged
In the upper surface of each electrode 34, upper cover body 37 is covered on the other end of the backing plate 36 relative to cell body 32, and lower cover 38 covers
The other end set on the lower surface of cell body 32 relative to upper cover body 37.
In the water tank 2 and electrolysis unit 3 that are completed, group install after electrolysis unit 3 anode strip 342 and cathode sheets
340 are locked on water tank lid 26 separately by two electrode columns 33.And detection device (such as flow rate detector 82) by through
Multiple cap bore 261 of water tank lid 26 are simultaneously set on water tank lid 26.Gasket 28 is arranged at water tank groove body 24, and passes through
The third embedded structure 282 of gasket 28 and the first embedded structure 246 of water tank groove body 24 are mutually chimeric.The of water tank groove body 24
One lateral margin 248 is covered in the second hollow portion 264 of water tank lid 26 by the second opening portion 266 of water tank lid 26, with
Water tank groove body 24 and water tank lid 26 are combined closely, and electrolysis unit 3 is vacantly fixedly arranged in water tank 2.Wherein, water tank 2
It is interconnected with electrolysis unit 3.
In the water tank 2, electrolysis unit 3, condensate filter 6 and the humidification device 9 that are completed, it is provided with electrolysis unit 3
Water tank 2 and condensate filter 6 are by the connection between the conduit 22 of water tank 2 and the blowhole 60 of condensate filter 6 with mutual
Connection.Then, the condensate filter 6 and humidification device 9 being interconnected with water tank be by the venthole 60 of condensate filter 6 with
Connection between second conduit 92 of humidification device 9 is to be interconnected.Further, in the 13rd specific embodiment, mist
Change/volatilization gas mixing channel 4 must be connected to the 4th conduit 98 of humidification device 9.
In practical application, water tank 2 is equipped with an electrolysis water W, and electrolysis unit 3 is set in water tank 2, to be electrolysed electrolysis
Water W is to generate a hydrogen and oxygen gas mixture G.The hydrogen and oxygen gas mixture G of electrode runner S1 is resulted from via corresponding backing plate 36
The first runner 370 of upper perforation 360 and corresponding upper cover body 37 is input to the first hollow portion 20.It is input to the first hollow portion
20 hydrogen and oxygen gas mixture G is further exported via the conduit 22 of water tank 2.The hydrogen-oxygen mixing exported by the conduit 22 of water tank 2
Gas G, which is obtained, to be condensed and is filtered into condensate filter 6 via the blowhole 60 of condensate filter 6.Into condensate filter 6
Blowhole 60 hydrogen and oxygen gas mixture G can first pass through first filter screen 600 and filtering square 602 preliminarily filtered.It connects
, carrying out preliminarily filtered hydrogen and oxygen gas mixture G can be condensed further into circulatory flow 640, meanwhile, hydrogen-oxygen
Mixed gas G must be filtered by the activated carbon fiber and filtering material being set in runner 640a and can be adsorbed in impurity
In 640 in circulatory flow.Then, filtered hydrogen and oxygen gas mixture G must be exported by the venthole 62 of condensate filter 6 and be filtered
Hydrogen and oxygen gas mixture G afterwards.
Furthermore filtered hydrogen and oxygen gas mixture G must be input to humidifying by the second conduit 92 connecting with venthole 62
Device 9.By the second conduit 92 received filtered hydrogen and oxygen gas mixture G must pass through multiple nanometers of two efferent ducts 94 perforation
To be expelled in hollow body 90.In practical application, the multiple nanometers of perforation as possessed by the surface of efferent duct 94, obtain
It is refined for the hydrogen and oxygen gas mixture to input humidification device, to form diffluent bubble disintegration.Meanwhile it being placed in wet
Makeup is set the supplement water in 9 and is shaken by rocking equipment 95, is easily dissolved in the supplement water after shaking to allow gas to
In.Supplement water after wherein the above-mentioned hydrogen and oxygen gas mixture G be discharged by nanometer perforation must be shaken by rocking equipment 95 carries out
Humidifying is obtained and is sucked for user to generate the hydrogen and oxygen gas mixture after humidifying, and but not limited to this, in practical application
When, the hydrogen and oxygen gas mixture G after the humidifying exported by humidification device 9 can be further and via atomization/volatilization gas mixing channel 4
The atomization gas G2 of generation is mixed, and is sucked with forming health care gas for user.In addition, above-mentioned have nanometer perforation by surface
The hydrogen and oxygen gas mixture G that efferent duct is discharged also is obtained in conjunction with the supplement water after shaking via rocking equipment 95 to generate a hydrogen
Water H.It more particularly, is diffluent refinement by the hydrogen and oxygen gas mixture G that there is the efferent duct of nanometer perforation to be discharged on surface
Bubble, and the supplement water after shaking via rocking equipment 95 is easily gas to be made to be dissolved in supplement water therein.Therefore this hair is penetrated
Bright hydrogen or oxygen gas generator can generate the hydrogen water H of dissolution higher concentration hydrogen-oxygen.
In addition to this, in another embodiment, hydrogen and oxygen gas mixture caused by electrolysis water W is electrolysed via electrolysis unit 3
Humidification device 9 must be directly entered and carry out humidifying.Imply that the hydrogen and oxygen gas mixture for resulting from electrode runner S1 via corresponding pad
The first runner 370 of the upper perforation 360 of plate 36 and corresponding upper cover body 37 is input to the first hollow portion 20.It is input to first
The hydrogen and oxygen gas mixture of hollow portion 20 is further exported via the conduit 22 of water tank 2.The hydrogen-oxygen exported by the conduit 22 of water tank 2
Mixed gas, which is obtained, is input to humidification device 9 via the second conduit 92 by connecting with conduit 22 to generate the hydrogen after humidifying
Oxygen gas mixture, and obtain and sucked for user.But not limited to this, in practical application, after the humidifying exported by humidification device 9
Hydrogen and oxygen mixture physical efficiency further mix with the atomization gas generated via atomization/volatilization gas mixing channel 4, to form guarantor
Strong gas is sucked for user.In addition, the above-mentioned hydrogen and oxygen gas mixture G that by surface there is the efferent duct of nanometer perforation to be discharged is also
It obtains in conjunction with the supplement water after being shaken via rocking equipment 95 to generate a hydrogen water.
In addition, when electrolysis unit 3 suspend electrolysis electrolysis water to generate hydrogen and oxygen gas mixture when, the second water mercury device to
The gas inside water tank 2 is extracted so that its internal generation negative pressure.Supplement water W2 via the supplement input of third conduit 96 must pass through
Above-mentioned negative pressure is inputted back in the water tank 2 for being provided with electrolysis unit 3 by humidification device 9.More particularly, supplement water passes through humidifying
It connects to be input to condensation filtering by humidification device 9 between second conduit 92 of device 9 and the venthole 62 of condensate filter 6
Device 6.Further, the impurity being adsorbed in the circulatory flow 640 of condensate filter 6 can be by above-mentioned supplement water via entering
Stomata 60 and conduit 22 backwash to the water tank 2 for being provided with electrolysis unit 3, to restore the filter capacity of circulatory flow, prevent
The obstruction of circulatory flow and corrosion and the consumption for lowering electrolyte.In in practice, the present invention is (to be implied that impurity using supplement water
Electrolyte) it backwashes to the water tank 2 for being provided with electrolysis unit 3, it can carry out being electrolysed required electrolysis to provide electrolysis unit 3
Water.Further, the electrolysis water W of the first hollow portion 20 of supplement input water tank 2 must be via the lower cover 38 of electrolysis unit 3
Second flow channel 380 and multiple lower perforation 3202 are input to corresponding electrode runner S1, are electrolysed when institute to provide electrolysis unit 3
The electrolysis water W needed.
In terms of comprehensive, of the invention to focus on proposing a kind of gas generator, it includes electrolysis units and humidifying to fill
It sets.In gas generator of the invention, hydrogen and oxygen gas mixture caused by electrolysis unit can be carried out wet by humidification device
Change, to provide the hydrogen and oxygen gas mixture for being suitble to human body sucking.In addition, hydrogen and oxygen gas mixture caused by electrolysis unit can pass through
Humidification device must be regarded needed for user in practical application with generating the hydrogen water of hydrogen and oxygen gas mixture of dissolution higher concentration
To generate the hydrogen water of the hydrogen and oxygen gas mixture with required concentration.In addition, design through the invention can be to supplement
Water-filling, while electrolyte being backwashed to electrolysis unit, to restore the filter capacity of circulatory flow, prevent the obstruction of circulatory flow
With the consumption for corroding and lowering electrolyte.
Finally, please referring to Figure 18 A, Figure 18 B, Figure 19, Figure 20 A and Figure 20 B, Figure 18 A and Figure 18 B is to be painted gas of the invention
The schematic diagram of different perspectives of the body generator in the 15th specific embodiment, Figure 19 be painted gas generator of the invention in
Rearview in embodiment shown in Figure 18 A, Figure 20 A and Figure 20 B are to be painted in Figure 18 A illustrated embodiment only to have condensation filtering
The top view of device and water tank lid and the sectional view set is cutd open along the line D-D of the top view.In the 15th specific embodiment, this hair
Bright gas generator includes water tank, electrolysis unit, atomization/volatilization gas mixing channel, pumping plant, condensate filter, cooling
Device and humidification device.Since the structure of said elements designs in explanation made above, therefore do not repeat again herein.More into one
Step ground, compared to circulatory flow shown in Figure 14 B, in this present embodiment (Figure 20 B), circulatory flow 640 only passes through two groups of runners
640a forms the effect of can reach condensation, while the design of condensate filter 6 can be made simplified and cost reduction.In addition,
In this present embodiment, pumping plant 5 (not being illustrated in figure), condensate filter 6 and cooling device 7 are all integrated and are set to water tank 2
Lid on, make it at a modular design, while its design compared to the 14th specific embodiment can more save
Space.In addition, when modular water tank 2, pumping plant 5, condensate filter 6 and cooling device 7 are mixed with atomization/volatilization gas
When slot 4 and humidification device 9 assemble, the present invention can have the advantages that easy to assembly and pipeline simplifies, so that gas of the invention produces
The whole design of raw device more optimizes.
In an embodiment, when electrolysis unit is electrically connected with external power supply, the output voltage of power supply be about 17 volts (V) extremely
Between 27 volts (V), the output electric current of power supply is about 30 amperes (A) between 40 amperes (A), i.e., electrolysis unit about generates every point
Gas output between 1.5 liters to 4.0 liters of clock.About 1.5 volts of voltage of each group of electrode (between positive and negative anodes) when using
(V) between 3 volts (V), the voltage then used if any eight groups is between 12V~24V.But not limited to this, in practical application
When, when electrolysis unit is electrically connected with external power supply, the output voltage of power supply is about 5 volts (V) between 24 volts (V), power supply
Output electric current be about 2 amperes (A) between 150 amperes (A), i.e. the power of electrolysis unit be about 10 watts (i.e. about 5V*2A) extremely
Between 3600 watts (i.e. about 24V*150A), electrolysis unit can generate the gas output between 0.01 liter to 12 liters per minute.
In conclusion gas generator of the present invention can save space using the design that electrolysis unit is set to water tank, simultaneously
For the hydrogen and oxygen gas mixture that electrolysis unit generates by riddling the electrolysis water of the first hollow portion of water tank, can pass through reduces air cavity
It is present in water tank, the temperature of electrolysis unit can also be made to reduce, to prevents the generation of gas explosion.Furthermore electrolysis of the invention
The gas vent of device and water inlet design, and the electrolysis water in water tank is allowed to be supplemented to electrolysis unit, and electrolysis unit institute
The hydrogen and oxygen gas mixture of generation can be discharged water tank, so as to reaching air water circulation.Furthermore pumping plant of the invention, water tank
It is designed with the structure that electrolysis unit is interconnected, the electrolysis water being placed in the first hollow portion can be made to carry out forced circulation, make water
Air cavity in case levels off to zero, to prevent the generation of gas explosion.
By the above detailed description of preferred embodiments, it is intended to more clearly describe feature and spirit of the invention,
And not scope of the invention is limited with above-mentioned disclosed preferred embodiment.On the contrary, the purpose is to uncommon
Various changes can be covered and have being arranged in the scope of the scope of the patents to be applied of the invention of equality by hoping.Although of the invention
Disclosed above with embodiment, however, it is not to limit the invention, any to be familiar with this those skilled in the art, of the invention not departing from
In spirit and scope, when can be used for a variety of modifications and variations, therefore protection scope of the present invention is when view appended claims
Subject to the range defined.
Claims (6)
1. a kind of gas generator, which is characterized in that it includes:
One water tank has one first hollow portion, which is equipped with an electrolysis water；And
One electrolysis unit is set within first hollow portion of the water tank and receives the electrolysis water of the water tank, the electrolysis unit
Comprising a cell body to separate the inner space of the electrolysis unit and first hollow portion of the water tank, the electrolysis unit to
The electrolysis water is electrolysed to generate a hydrogen and oxygen gas mixture；Wherein the electrolysis unit includes multiple electrodes and a backing plate, the multiple
Electrode, which is respectively separated, is set within the cell body and is formed multiple electrodes runner, which is set to the multiple electrode stream
On road and there are multiple upper perforation, and the multiple electrode runner is connected to by the multiple upper perforation with first hollow portion；
The cell body has a lower surface, and the lower surface of the cell body has multiple lower perforation, and the multiple electrode runner
It is connected to by the multiple lower perforation with first hollow portion；
One pumping plant is placed in the electrolysis water in first hollow portion to forced circulation；
One power supply, wherein the multiple electrode includes a cathode sheets, an anode strip and multiple bipolar electrode pieces, it is the multiple
Bipolar electrode piece is arranged at intervals between the cathode sheets and the anode strip, which is connected to the cathode of the power supply, should
Anode strip is connected to the anode of the power supply；And
One atomization/volatilization gas mixing channel, wherein the atomization/volatilization gas mixing channel receives the hydrogen and oxygen gas mixture, and the atomization/
Volatilization gas mixing channel generates an atomization gas and mixes with the hydrogen and oxygen gas mixture, is inhaled with forming a health care gas for a user
Enter, wherein the atomization gas is selected from one by water vapour, atomization liquid medicine, volatile spirits and combinations thereof, in composed group
Kind.
2. gas generator according to claim 1, which is characterized in that the hydrogen and oxygen gas mixture is exported to the water tank, should
Water tank separately has a conduit to export the hydrogen and oxygen gas mixture, mixes so that the atomization/volatilization gas mixing channel receives the hydrogen-oxygen
Close gas.
3. gas generator according to claim 2, which is characterized in that when the electrolysis unit suspend be electrolysed the electrolysis water with
When generating the hydrogen and oxygen gas mixture, which can be used to supplement to input the electrolysis water.
4. gas generator according to claim 3, which is characterized in that the pumping plant includes a water inlet pipe and a water outlet
Pipe, the water tank include a water outlet and a water inlet, and water outlet and the water inlet of the water tank are connected by first hollow portion
It is logical, the outlet pipe of the pumping plant and the water inlet of the water tank be connected with each other and the water inlet pipe of the pumping plant with
The water outlet of the water tank is connected with each other.
5. gas generator according to claim 1, which is characterized in that be made of two adjacent bipolar electrode pieces
The voltage difference of one group of electrolysis electrode is between 1.5V~3V.
6. gas generator according to claim 5, which is characterized in that the electrolysis water fill the water tank this is first hollow
The water level in portion is higher than the 90% of full-water level.
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| TW103135890 | 2014-10-16 | ||
| TW103135890A TWI586841B (en) | 2014-10-16 | 2014-10-16 | A gas generator |
| CN201410620116.5A CN105624724B (en) | 2014-10-16 | 2014-11-05 | Gas generator |
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| CN106435633B (en) * | 2015-08-11 | 2018-11-16 | 林信涌 | Gas generator |
| CN108796533B (en) * | 2017-05-04 | 2020-09-25 | 林信涌 | Gas generator |
| CN109385642B (en) | 2017-08-04 | 2021-04-13 | 林信涌 | Gas generator |
| CN112013705A (en) * | 2019-05-28 | 2020-12-01 | 上海潓美医疗科技有限公司 | Radiator and hydrogen generator with radiating function |
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Also Published As
| Publication number | Publication date |
|---|---|
| CN109082679B (en) | 2020-05-29 |
| TW201615893A (en) | 2016-05-01 |
| CN105624724A (en) | 2016-06-01 |
| CN105624724B (en) | 2018-09-14 |
| TWI586841B (en) | 2017-06-11 |
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