CN105498065A - Gas generator - Google Patents
Gas generator Download PDFInfo
- Publication number
- CN105498065A CN105498065A CN201410618949.8A CN201410618949A CN105498065A CN 105498065 A CN105498065 A CN 105498065A CN 201410618949 A CN201410618949 A CN 201410618949A CN 105498065 A CN105498065 A CN 105498065A
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- China
- Prior art keywords
- hydrogen
- electrolysis
- gas mixture
- oxygen gas
- water tank
- Prior art date
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- 238000005868 electrolysis reaction Methods 0.000 claims abstract description 330
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 325
- 239000007789 gas Substances 0.000 claims abstract description 187
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 185
- 239000001257 hydrogen Substances 0.000 claims abstract description 184
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 claims abstract description 162
- 229910001882 dioxygen Inorganic materials 0.000 claims abstract description 162
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims abstract description 161
- 239000000203 mixture Substances 0.000 claims description 165
- 239000012267 brine Substances 0.000 claims description 106
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 claims description 106
- 238000000889 atomisation Methods 0.000 claims description 69
- 230000001502 supplementing effect Effects 0.000 claims description 55
- 238000002156 mixing Methods 0.000 claims description 35
- 238000001914 filtration Methods 0.000 claims description 34
- 150000002431 hydrogen Chemical class 0.000 claims description 23
- 230000036541 health Effects 0.000 claims description 20
- 239000012535 impurity Substances 0.000 claims description 17
- 238000009833 condensation Methods 0.000 claims description 13
- 230000005494 condensation Effects 0.000 claims description 13
- 239000003814 drug Substances 0.000 claims description 7
- 239000007788 liquid Substances 0.000 claims description 6
- 235000015096 spirit Nutrition 0.000 claims description 6
- 239000013589 supplement Substances 0.000 claims description 5
- 230000009514 concussion Effects 0.000 claims description 3
- 239000001301 oxygen Substances 0.000 abstract description 8
- 229910052760 oxygen Inorganic materials 0.000 abstract description 8
- 210000005056 cell body Anatomy 0.000 description 68
- 238000005086 pumping Methods 0.000 description 50
- 238000013461 design Methods 0.000 description 32
- 230000000007 visual effect Effects 0.000 description 24
- 238000010586 diagram Methods 0.000 description 22
- 238000007789 sealing Methods 0.000 description 12
- 239000011148 porous material Substances 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
- 239000000463 material Substances 0.000 description 6
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 6
- 150000001875 compounds Chemical class 0.000 description 5
- 238000001816 cooling Methods 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
- 238000005422 blasting Methods 0.000 description 4
- 230000007797 corrosion Effects 0.000 description 4
- 238000005260 corrosion Methods 0.000 description 4
- 238000005304 joining Methods 0.000 description 4
- 230000005855 radiation Effects 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 230000008901 benefit Effects 0.000 description 3
- 201000010099 disease Diseases 0.000 description 3
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000002360 explosive Substances 0.000 description 3
- 239000000284 extract Substances 0.000 description 3
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical class C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 3
- 238000003825 pressing Methods 0.000 description 3
- 150000003254 radicals Chemical class 0.000 description 3
- 208000017667 Chronic Disease Diseases 0.000 description 2
- 208000027418 Wounds and injury Diseases 0.000 description 2
- 230000032683 aging Effects 0.000 description 2
- 230000003064 anti-oxidating effect Effects 0.000 description 2
- 229910000019 calcium carbonate Inorganic materials 0.000 description 2
- 230000006378 damage Effects 0.000 description 2
- 208000014674 injury Diseases 0.000 description 2
- 210000004072 lung Anatomy 0.000 description 2
- 238000000034 method Methods 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
- 229910001316 Ag alloy Inorganic materials 0.000 description 1
- 229910000838 Al alloy Inorganic materials 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
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 1
- 206010028980 Neoplasm Diseases 0.000 description 1
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 1
- 230000004308 accommodation Effects 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- 230000003078 antioxidant effect Effects 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 201000011510 cancer Diseases 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000002512 chemotherapy Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 238000009795 derivation Methods 0.000 description 1
- 230000037213 diet Effects 0.000 description 1
- 235000005911 diet Nutrition 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 235000013402 health food Nutrition 0.000 description 1
- 239000002075 main ingredient Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000010453 quartz Substances 0.000 description 1
- 238000011160 research Methods 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
- 238000003860 storage Methods 0.000 description 1
- 208000024891 symptom Diseases 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
Landscapes
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Abstract
The invention discloses a gas generator, which comprises an electrolysis device and a humidifying device. The electrolysis device is used for electrolyzing the electrolyzed water to generate hydrogen-oxygen mixed gas. The humidifying device comprises: the hollow body is used for accommodating supplementary water; the second conduit is used for receiving the mixed hydrogen and oxygen gas; and at least one output pipe with a plurality of through holes on the surface is connected with the second conduit. When the electrolysis device electrolyzes water to generate hydrogen-oxygen mixed gas, the hydrogen-oxygen mixed gas is discharged through a plurality of perforations of at least one output pipe to humidify the hydrogen-oxygen mixed gas to provide gas suitable for human body inhalation.
Description
Technical field
The invention relates to a kind of gas generator, relate to a kind of gas generator with humidification function especially.
Background technology
All the time, the mankind are pay attention to completely for life, and the exploitation of the technology of many medical treatment, is all used to anti-disease, to continue the life of the mankind.The medical mode major part in past is all belong to passive, namely when disease occurs, then carries out medical treatment to the ill, the chemotherapy of such as operation, administration, even cancer, the taking good care of of radiation treatment or chronic disease, rehabilitation, rectification etc.But in recent years, many medical experts study towards preventative medical procedures gradually, the research of such as health food, hereditary screening with prevent ahead of time, especially active the morbidity possible for futurity prevent.In addition, in order to extend human longevity, many aging resistance, antioxidative technology are developed gradually, and are adopted by masses widely, comprise the skin care products and antioxidation foodstuff/medicine etc. smeared.
After deliberation find: human body because of a variety of causes, (such as disease, diet, residing environment or living habit) the unease oxygen (O+) of derivation, also known as free radical (harmful free radicals), the water of part can be mixed into the hydrogen sucked, and excrete.The quantity of indirect minimizing human free radical, reaches acidic physique and is reduced to healthy alkaline body constitution, can antioxidation, aging resistance, and then also reaches and eliminate chronic disease and aesthetic health care effect.Even have clinical experiment to show, for the patient of some lying on bed for a long time sick beds, because breathe high concentration oxygen for a long time, the injury of lung caused, can through suction hydrogen to alleviate the symptom of injury of lung.
But usually have higher temperature and relatively dry via the hydrogen and oxygen gas mixture produced after electrolysis unit electrolysis brine electrolysis, it is also not suitable for human body and directly sucks.Meanwhile, in electrolytic process, also have the problem of brine electrolysis and electrolyte consumption, and need supplementing water and electrolytical situation to occur.Above problem so usually cause known electrolysis unit use on not convenient.
Summary of the invention
Therefore, one of viewpoint of the present invention is to provide a kind of gas generator, and it comprises an electrolysis unit and a humidification device.Electrolysis unit is equipped with a brine electrolysis, in order to electrolysis brine electrolysis to produce a hydrogen and oxygen gas mixture.Humidification device includes a hollow body, an input pipe and at least one outlet tube.Hollow body is in order to an accommodating supplementing water.Second conduit is in order to receive hydrogen and oxygen gas mixture.At least one outlet tube and the second tubes connection.The surface of at least one outlet tube has multiple perforation.Wherein when electrolysis unit electrolysis brine electrolysis is to produce hydrogen and oxygen gas mixture, hydrogen and oxygen gas mixture is discharged via multiple perforation of at least one outlet tube, with this hydrogen and oxygen gas mixture of humidifying.
Humidification device optionally separately comprises a rocking equipment.Rocking equipment is in order to shake supplementing water.Supplementing water after rocking equipment concussion is in order to humidified hydrogen oxygen gas mixture.Supplementing water after hydrogen and oxygen gas mixture can shake with rocking equipment is combined, and then produces hydrogen water.
Humidification device optionally separately includes one the 3rd conduit.3rd conduit is arranged on hollow body, in order to export hydrogen water.
When electrolysis unit suspends electrolysis brine electrolysis to produce hydrogen and oxygen gas mixture, humidification device is supplementary supplementing water optionally, and via the 3rd conduit of humidification device to input supplementing water in the hollow body of humidification device.
Humidification device optionally separately includes one the 4th conduit.4th conduit is arranged on hollow body, in order to export the hydrogen and oxygen gas mixture after humidifying.
Moreover gas generator of the present invention separately can comprise one atomization/volatilization gas mixing channel.Atomization/volatilization gas mixing channel connects the 4th conduit of humidification device, in order to receive the hydrogen and oxygen gas mixture after humidifying.Atomization/volatilization gas mixing channel produces an atomization gas and mixes with the hydrogen and oxygen gas mixture after humidifying, sucks for a user to form a health care gas.Wherein atomization gas is selected from the one in the group be made up of water vapour, atomization liquid medicine, volatile spirits and combination thereof.
Gas generator of the present invention separately can comprise a hand-held atomising device.Hand-hold atomization device connects the 4th conduit of humidification device, in order to receive the hydrogen and oxygen gas mixture after humidifying.Hand-hold atomization device produces an atomization gas and mixes with the hydrogen and oxygen gas mixture after humidifying, sucks for a user to form a health care gas.Wherein atomization gas is selected from the one in the group be made up of water vapour, atomization liquid medicine, volatile spirits and combination thereof.
Moreover gas generator of the present invention can separately comprise a condensate filter.Condensate filter is located between electrolysis unit and humidification device, the hydrogen and oxygen gas mixture produced in order to condensation electrolysis unit the impurity filtered in hydrogen and oxygen gas mixture.Condensate filter has a blowhole and a venthole.Blowhole is connected to electrolysis unit, in order to receive hydrogen and oxygen gas mixture.Venthole is in order to discharge the hydrogen and oxygen gas mixture after filtering.Wherein the second tubes connection of humidification device is in the venthole of condensate filter, in order to the hydrogen and oxygen gas mixture after receiving filtration.
When electrolysis unit suspends electrolysis brine electrolysis to produce hydrogen and oxygen gas mixture, humidification device is supplementary supplementing water optionally, and via the second conduit of humidification device and the venthole of condensate filter to input supplementing water.Impurity can also be backwashed to electrolysis unit by the blowhole of supplementing water via condensate filter.
The generation flow rate of the hydrogen and oxygen gas mixture of gas generator is optionally between 0.01L/min. and 12L/min..
The aperture of multiple perforation can between the scope of 2 nanometer to 10 nanometers.
Rocking equipment can comprise a sonicator to shake supplementing water.
Rocking equipment can comprise a centrifugeblade and connect a CD-ROM drive motor of centrifugeblade.CD-ROM drive motor drives centrifugeblade to rotate to shake supplementing water and centrifugal.
Comprehensive, of the present invention focusing on proposes a kind of gas generator, and it comprises electrolysis unit and humidification device.In gas generator of the present invention, the hydrogen and oxygen gas mixture that electrolysis unit produces can carry out humidifying by humidification device, with the hydrogen and oxygen gas mixture providing applicable human body to suck.In addition, the hydrogen and oxygen gas mixture that electrolysis unit produces can pass through humidification device, to produce the hydrogen water of the hydrogen and oxygen gas mixture dissolving higher concentration, when practical application, visual user is required to produce the hydrogen water with the hydrogen and oxygen gas mixture of desired concn.In addition, can in order to supplementary supplementing water, and electrolyte be backwashed to electrolysis unit by design of the present invention, in order to recover circulatory flow filter capacity, prevent the obstruction of circulatory flow and corrosion and lower electrolytical consumption.
Accompanying drawing explanation
Figure 1A and Figure 1B is the schematic diagram illustrating the different visual angles of gas generator of the present invention in the first specific embodiment;
Fig. 2 A and Fig. 2 B is the schematic diagram of different visual angles when only having tank upper cover and electrolysis unit combination in Figure 1A illustrated embodiment;
Fig. 3 A and Fig. 3 B is the schematic diagram of different visual angles when only having electrolysis unit and the combination of water tank cell body in Figure 1A illustrated embodiment;
Fig. 4 A and Fig. 4 B is the explosive view of the electrolysis unit different visual angles in Figure 1A illustrated embodiment illustrating gas generator of the present invention;
Fig. 5 A and Fig. 5 B illustrates the water tank cell body of gas generator of the present invention and the top view of electrolysis unit in embodiment shown in Fig. 3 A and the A-A line along this top view to cut open the profile established;
Fig. 6 is the schematic diagram of different visual angles when only having cell body, dividing plate and combination of electrodes in Figure 1A illustrated embodiment;
Fig. 7 A and Fig. 7 B illustrates the water tank cell body of gas generator of the present invention and the top view of electrolysis unit in embodiment shown in Fig. 3 A and the B-B line along this top view to cut open the profile established;
Fig. 8 illustrates the schematic diagram of gas generator of the present invention in the second specific embodiment;
Fig. 9 A and Fig. 9 B is the schematic diagram illustrating the different visual angles of gas generator of the present invention in the tenth specific embodiment;
Figure 10 A and Figure 10 B is the schematic diagram of different visual angles when only having condensate filter and water tank cover assembling in Fig. 9 A illustrated embodiment;
Figure 11 illustrates in Figure 10 A illustrated embodiment schematic diagram when not having water tank lid;
Figure 12 be illustrate embodiment illustrated in fig. 11 in schematic diagram when not there is drainage screen;
Figure 13 be illustrate embodiment illustrated in fig. 12 in do not have filter square time schematic diagram;
Figure 14 A and Figure 14 B illustrates the top view of condensate filter in embodiment shown in Figure 10 A of gas generator of the present invention and the C-C line along this top view cuts open the profile established;
Figure 15 A and Figure 15 B is the schematic diagram illustrating the different visual angles of gas generator of the present invention in the 14 specific embodiment;
Figure 16 illustrates the schematic diagram only in Figure 15 A illustrated embodiment with humidification device;
Figure 17 illustrates the schematic diagram of gas generator of the present invention in the 5th specific embodiment;
Figure 18 A and Figure 18 B is the schematic diagram illustrating the different visual angles of gas generator of the present invention in the 15 specific embodiment;
Figure 19 illustrates the rearview of gas generator of the present invention in embodiment shown in Figure 18 A;
Figure 20 A and Figure 20 B illustrates the top view only in Figure 18 A illustrated embodiment with condensate filter and water tank lid and cuts open along the D-D line of this top view the profile established.
About advantage of the present invention, spirit and feature, with embodiment and with reference to appended accompanying drawing, will be described in detail and discussion.
[symbol description]
W: brine electrolysis W2: supplementing water
G: hydrogen and oxygen gas mixture G2: atomization gas
H: hydrogen water
1: gas generator 2: water tank
20: the first hollow bulbs 200: top
202: bottom 22: conduit
24: water tank cell body 240: the first base
242: the first wall portion 244: the first peristomes
246: the first embedded structure 248: the first lateral margins
249a: outlet 249b: water inlet
26: water tank lid 260: the second base
261: cap bore 262: the second wall portion
264: the second hollow bulb 266: the second peristomes
28: sealing gasket 280: the three peristome
282: the three embedded structures 3: electrolysis unit
30: dividing plate 300: intercommunicating pore
32: cell body 320: the four base
3202: lower perforation 3204: groove
322: fourth wall 3220: fixed leg
324: the four hollow bulb 326: the four peristomes
33: electrode column 34: multiple electrode
340: cathode sheets 342: anode strip
344: bipolar electrode sheet 36: backing plate
360: upper perforation 37: upper cover body
370: first flow 38: lower cover
380: the second runners 4: atomization/volatilization gas mixing channel
5: pumping plant 50: oral siphon
52: outlet pipe 6: condensate filter
60: blowhole 600: drainage screen
602: filter square 62: venthole
64: condensate film 640: circulatory flow
640a: runner 642: gradual-enlargement type runner
644: be communicated with runner 7: chiller
70: radiator 700: casing
702: radiating tube 704: entrance
706: outlet 72: fan
82: flow rate detector 9: humidification device
90: hollow body 92: the second conduit
94: outlet tube 95: rocking equipment
96: the three conduit 98: the four conduits
Detailed description of the invention
In order to allow advantage of the present invention, spirit and feature can more easily and be expressly understood that, follow-uply will carry out describing with reference to appended accompanying drawing with embodiment and discuss.It should be noted that these embodiments are only the representational embodiment of the present invention, wherein illustrated ad hoc approach, device, condition, material etc. are also not used to the embodiment limiting the present invention or correspondence.
First, the present invention proposes a kind of gas generator, and it is a kind of protected against explosion gas generator.Refer to Figure 1A, Figure 1B, Fig. 2 A and Fig. 2 B, Figure 1A and Figure 1B is the schematic diagram illustrating the different visual angles of gas generator of the present invention in the first specific embodiment, Fig. 2 A and Fig. 2 B is the schematic diagram of different visual angles when only having tank upper cover and electrolysis unit combination in Figure 1A illustrated embodiment, as shown in the figure, in the first embodiment, gas generator 1 of the present invention includes water tank 2 and electrolysis unit 3.Water tank 2 is equipped with a brine electrolysis W, and electrolysis unit 3 is arranged in water tank 2, in order to this brine electrolysis of electrolysis W to produce a hydrogen and oxygen gas mixture G.Wherein, when electrolysis unit operates, the water level of the first hollow bulb Inner electrolysis water of water tank is between 90% ~ 100% full-water level.In an embodiment, when electrolysis unit 3 starts electrolysis brine electrolysis W, brine electrolysis W riddles the first hollow bulb of water tank 2 and is in full-water level, and when after electrolysis unit 3 electrolysis brine electrolysis W, brine electrolysis W fills the water level of the first hollow bulb of water tank 2 higher than 90% of full-water level.First be described to the design of each element of the present invention respectively below.
First, water tank 2 of the present invention has one first hollow bulb 20 and a conduit 22.First hollow bulb 20 of water tank 2 is suitable for accommodation one brine electrolysis W.Brine electrolysis W Main Ingredients and Appearance is pure water, optionally can add a small amount of electrolyte, as sodium hydroxide, calcium carbonate, sodium chloride etc.The conduit 22 of water tank 2 is be interconnected with the first hollow bulb 20 of water tank 2, and the hydrogen and oxygen gas mixture G produced by electrolysis unit 3 in order to output and supplementary this brine electrolysis of input W is in water tank 2.
Further, the explosive view that Fig. 3 A and Fig. 3 B, Fig. 3 A and Fig. 3 B is the water tank different visual angles in specific embodiment shown in Figure 1A illustrating gas generator of the present invention is referred to.In the present embodiment, water tank 2 separately includes water tank cell body 24 and a water tank lid 26.
Water tank cell body 24 is roughly divided into one first base 240 and one first wall portion 242.First wall portion 242 forms toward extension toward its normal vector direction from the inner surface of the first base 240, and the first wall portion 242 is arranged with the first hollow bulb 20, and this first hollow bulb 20 is have one first peristome 244 relative to the other end of the first base 240.Meanwhile, and the first wall portion 242 is have one first lateral margin 248 relative to the opposite side of the first base 240, and this first lateral margin 248 is then around aforesaid first peristome 244.Further, the water tank cell body 24 of water tank 2 separately comprises an an outlet 249a and water inlet 249b.In the present embodiment, the outlet 249a of water tank cell body 24 is the first wall portion 242 two surfaces relative to electrolysis unit 3 direction of joining water box cell body 24, and the water inlet 249b of water tank cell body 24 is the first wall portion 242 two surfaces relative to electrolysis unit 3 direction of joining water box cell body 24.Wherein, the outlet 249a of water tank cell body 24 and the water inlet 249b of water tank cell body 24 are communicated with by the first hollow bulb 20.The outlet 249a of a water tank cell body 24 and water inlet 249b can be interconnected with the first hollow bulb 20 for a pumping plant and water tank 2.
Water tank lid 26 is roughly divided into one second base 260 and one second wall portion 262.Second wall portion 262 forms toward extension toward its normal vector direction from the inner surface of the second base 260, and the second wall portion 262 is that to be arranged with one second hollow bulb 264, the second hollow bulb 264 relative to the other end of the second base 260 be have one second peristome 266.Water tank lid 26 is covered in the second hollow bulb 264 by first lateral margin 248 of the second peristome 266 by water tank cell body 24.On the second base 260 that conduit 22 can be arranged at water tank lid 26 and the second base 260 of joining water box lid 26 relative to two surfaces in water tank cell body 24 direction, but it is not as limit, when practical application, the element that conduit 22 can also have an input/output function by a guide hole or other replaced.Water tank lid 26 separately includes multiple cap bore (as shown in Figure 10 A), second base 260 of multiple cap bore joining water box lid 26 is surperficial relative to two of water tank cell body 24 direction, electrode column in order to electrolysis device 3 runs through and is arranged at electrolysis unit 3, or runs through with for checkout gear (as flow rate detector, water-level gauge, relief valve) and arrange thereon.
Further, in the present embodiment, water tank 2 separately includes a sealing gasket 28, and it is arranged between water tank cell body 24 and water tank lid 26, combines closely in order to make water tank cell body 24 and water tank lid 26.Sealing gasket 28 has one the 3rd peristome 280.When sealing gasket 28 is arranged between water tank cell body 24 and water tank lid 26, the 3rd peristome 280 of sealing gasket 28 is located in wherein multiple cap bore 261 and the second peristome 266.The corresponding surface of water tank cell body 24 and sealing gasket 28 more can have one first embedded structure 246 and the 3rd corresponding embedded structure 282 respectively and be able to mutually chimeric both it.First embedded structure 246 is located in wherein by the first peristome 244.3rd embedded structure 282 is located in wherein by the 3rd peristome 280.
Then, the explosive view that Fig. 4 A and Fig. 4 B, Fig. 4 A and Fig. 4 B is the electrolysis unit different visual angles in Figure 1A illustrated embodiment illustrating gas generator of the present invention is referred to.Electrolysis unit 3 comprises a cell body 32, multiple electrode 34, backing plate 36, upper cover body 37 and lower cover 38.Wherein multiple electrode 34 to be arranged at intervals at respectively within cell body 32 and to form multiple electrode runner S1.Backing plate 36 is arranged at the upper surface of each electrode 34.Upper cover body 37 is covered on the other end of backing plate 36 relative to cell body 32.Lower cover 38 is covered on the other end of lower surface relative to upper cover body 37 of cell body 32.
Further, refer to Fig. 5 A and five B, Fig. 5 A and Fig. 5 B to illustrate the water tank cell body of gas generator of the present invention and the top view of electrolysis unit in the embodiment of embodiment shown in Fig. 3 A and the A-A line along this top view to cut open the profile established.Electrolysis unit separately has a dividing plate 30.Dividing plate 30 forms toward extension toward its normal vector direction from the side surface of cell body relative to water tank 2, in order to the first hollow bulb 20 of water tank 2 is separated into top 200 and a bottom 202.Dividing plate 30 comprises an intercommunicating pore 300.Intercommunicating pore 300 is communicated with two surfaces of dividing plate 30 relative to the first base 240 direction of water tank cell body 24.The top 200 of the first hollow bulb 20 and bottom 202 are interconnected by intercommunicating pore.But the design of intercommunicating pore does not illustrate with this enforcement and is limited, when practical application, in all visual use of the quantity of intercommunicating pore or external form, actual demand selects design voluntarily.
Then, refer to Fig. 6, Fig. 6 is the schematic diagram of different visual angles when only having cell body, dividing plate and combination of electrodes in Figure 1A illustrated embodiment.Cell body 32 is roughly divided into one the 4th base 320 and a fourth wall 322.Fourth wall 322 forms toward extension toward its normal vector direction from the inner surface of the 4th base 320, and fourth wall 322 is arranged with the 4th hollow bulb 324, and the 4th hollow bulb 324 is have one the 4th peristome 326 relative to the other end of the 4th base 320.4th hollow bulb 324 is suitable for accommodating this brine electrolysis W.In addition, in order to express the design of cell body of the present invention, be the multiple electrodes deliberately economized slightly wherein in Fig. 6, but when practical application, in visual use, actual demand select design voluntarily.
Then, refer to Fig. 5 A, Fig. 5 B, Fig. 6, Fig. 7 A and Fig. 7 B, Fig. 7 A and Fig. 7 B illustrate the water tank cell body of gas generator of the present invention and the top view of electrolysis unit in embodiment shown in Fig. 3 A and the B-B line along this top view to cut open the profile established.In the present embodiment, the lower surface of cell body 32 is the 4th base 320 of cell body 32.4th base 320 of cell body 32 has multiple lower perforation 3202.Multiple lower perforation 3202 is communicated with two surfaces of the 4th base 320 relative to the first base 240 direction of water tank cell body 24 of cell body 32.4th base 320 of cell body 32 separately has multiple groove 3204.Multiple groove 3204 forms along normal vector direction toward interior extension relative to the surface of the 4th peristome 326 from the 4th base 320 of cell body 32.Each groove 3204 is that compartment of terrain is between lower perforation 3202 and adjacent lower perforation 3202.Multiple groove 3204 can in order to electrodes 34.Meanwhile, the fourth wall 322 of cell body 32 separately has multiple fixed leg 3220.Multiple fixed leg 3220 forms toward extension toward its normal vector direction from the surface of fourth wall 322 relative to multiple lower perforation 3202.Fixed leg 3220 and adjacent fixed leg 3220 can in order to the electrode 34 of fixed placement in groove 3204.When being fixed between fixed leg 3220 and adjacent fixed leg 3220, multiple electrode runner S1 being formed within cell body 32 in the groove 3204 that multiple electrode 34 is arranged at intervals at cell body 32 respectively.Wherein each electrode runner S1 can be communicated with by the bottom 202 of corresponding lower perforation 3202 with the first hollow bulb 20 independently of one another.
Backing plate 36 has multiple upper perforation 360.Multiple upper perforation 360 is communicated with two surfaces of backing plate 36 relative to cell body 32 direction.Further, each electrode runner S1 also can be communicated with by the top 200 of corresponding upper perforation 360 with the first hollow bulb 20 independently of one another.
Multiple electrode 34 includes cathode sheets 340, anode strip 342 and multiple bipolar electrode sheet 344.Multiple bipolar electrode sheet 344 is arranged at intervals between cathode sheets 340 and anode strip 342.In the present embodiment, electrolysis unit 3 separately comprises two electrode columns 33, in order to lock anode strip 342 and cathode sheets 340 respectively on water tank lid 26, to be fixedly arranged on vacantly in water tank 2 by electrolysis unit 3.Further, in the present embodiment, gas generator 1 separately comprises a power supply (not being illustrated in figure).Cathode sheets 340 can be connected to the negative pole of power supply, and anode strip 342 can be connected to the positive pole of power supply, and the voltage difference of the one group of electrolysis electrode be wherein made up of two adjacent bipolar electrode sheets is about between 1.5V ~ 3V.In an embodiment, the voltage difference of one group of electrolysis electrode that cathode sheets 340 and bipolar electrode sheet 344 are formed is about between 1.5V ~ 3V.In another embodiment, the voltage difference of one group of electrolysis electrode that bipolar electrode sheet 344 and adjacent bipolar electrode sheet 344 are formed is about between 1.5V ~ 3V.In another embodiment, the voltage difference of one group of electrolysis electrode that bipolar electrode sheet 344 and anode strip 342 are formed is about between 1.5V ~ 3V.
Upper cover body 37 comprises at least one first flow 370.As shown in Figure 4 B, first flow 370 forms toward interior extension along normal vector direction from the surface of upper cover body 37 relative to backing plate 36.The multiple upper perforation 360 and the first hollow bulb 20 that are positioned at backing plate 36 are interconnected by described at least one first flow 370.
Lower cover 38 comprises at least one second runner 380.As shown in Figure 4 A, the second runner 380 forms toward interior extension along normal vector direction from the surface of lower cover 38 relative to the 4th base 320 of cell body 32.The multiple lower perforation 3202 being positioned at the 4th base 320 of cell body 32 is be interconnected by described at least one second runner 380 with this first hollow bulb 20.
Further, please first consult Fig. 8, Fig. 8 illustrates the schematic diagram of gas generator of the present invention in the second specific embodiment.In the second specific embodiment, gas generator 1 of the present invention separately comprises a pumping plant 5 (only illustrating with dotted line in Fig. 8).Pumping plant 5 can be placed in the first hollow bulb 20 and interior brine electrolysis W in order to forced circulation.Pumping plant 5 comprises oral siphon 50 and an outlet pipe 52.The outlet pipe 52 of pumping plant 5 is interconnected in order to the water inlet 249b of feed pump device 5 with this water tank 2.The oral siphon 50 of pumping plant 5 is interconnected in order to the outlet 249a of feed pump device 5 with this water tank 2.
Further, in the 3rd specific embodiment, gas generator 1 of the present invention separately comprises one atomization/volatilization gas mixing channel 4 (as shown in fig. 15).Atomization/volatilization gas mixing channel 4 can be connected to electrolysis unit 3, in order to receive hydrogen and oxygen gas mixture G.Atomization/volatilization gas mixing channel 4 can produce an atomization gas G2 and mix with hydrogen and oxygen gas mixture G, sucks for this user to form a health care gas.When practical application, atomization gas G2 can be selected from by water vapour, atomization liquid medicine, volatile spirits and combination thereof, the one in the group formed.
Above, after each design of each element is described, below the compound mode of each element to a kind of gas generator and its application are described.
In the electrolysis unit 3 assembled, multiple electrode 34 is arranged at intervals at cell body 32 respectively, backing plate 36 is arranged at the upper surface of each electrode 34, upper cover body 37 is covered on the other end of backing plate 36 relative to cell body 32, and lower cover 38 is covered on the other end of lower surface relative to upper cover body 37 of cell body 32.
In the water tank 2 assembled and electrolysis unit 3, the anode strip 342 of the electrolysis unit 3 after having assembled and cathode sheets 340 are locked on water tank lid 26 separately by two electrode columns 33.And checkout gear (as flow rate detector 82) by through water tank lid 26 multiple cap bore 261 and be arranged on water tank lid 26.Sealing gasket 28 is arranged at water tank cell body 24, and is mutually fitted together to by the 3rd embedded structure 282 of sealing gasket 28 and the first embedded structure 246 of water tank cell body 24.First lateral margin 248 of water tank cell body 24 is covered in the second hollow bulb 264 of water tank lid 26 by the second peristome 266 of water tank lid 26, water tank cell body 24 and water tank lid 26 to be combined closely, and is fixedly arranged on vacantly in water tank 2 by electrolysis unit 3.Wherein, water tank 2 and electrolysis unit 3 are interconnected.
Then, in the water tank 2 assembled, electrolysis unit 3 and pumping plant 5, water tank 2 and pumping plant 5 are to be interconnected by the connection of the outlet 249a of the outlet pipe 52 of pumping plant 5 and the connection of the water inlet 249a of water tank 5 and the oral siphon 50 of pumping plant 5 and water tank 5.Further, in the 3rd embodiment, atomization/volatilization gas mixing channel 4 connects electrolysis unit 3.
When practical application, water tank 2 is equipped with a brine electrolysis W, and electrolysis unit 3 is arranged in water tank 2, in order to this brine electrolysis of electrolysis W to produce a hydrogen and oxygen gas mixture G.The hydrogen and oxygen gas mixture G resulting from electrode runner S1 inputs to the first hollow bulb 20 via the upper perforation 360 of corresponding backing plate 36 and the first flow 370 of corresponding upper cover body 37.The hydrogen and oxygen gas mixture G inputing to the first hollow bulb 20 exports via the conduit 22 of water tank 2 further, and be available for users to suck, but not as limit, when practical application, input to the first hollow bulb 20 hydrogen and oxygen gas mixture G can further with via being atomized/atomization gas G2 that volatilization gas mixing channel 4 produces mixes, suck for user to form health care gas.
In addition, when electrolysis unit 3 suspends electrolysis brine electrolysis W to produce hydrogen and oxygen gas mixture G, conduit 22 can be used for supplementing input brine electrolysis W, is full of the first hollow bulb 20 and/or electrolysis unit 3 to make brine electrolysis W.Supplement the brine electrolysis W of input first hollow bulb 20 and can input to corresponding electrode runner S1 via the second runner 380 of the lower cover 38 of electrolysis unit 3 and multiple lower perforation 3202, brine electrolysis W required during to provide electrolysis unit 3 electrolysis.Wherein, when electrolysis unit operates, the water level of the first hollow bulb Inner electrolysis water is between 90% ~ 100% full-water level.Full-water level refers to that brine electrolysis is full of the first hollow bulb of water tank in one embodiment.In an embodiment, when electrolysis unit 3 starts electrolysis brine electrolysis W, brine electrolysis W be riddle water tank 2 the first hollow bulb and be in full-water level, when after electrolysis unit 3 electrolysis brine electrolysis W, brine electrolysis W fills the water level of the first hollow bulb of water tank 2 higher than 90% of full-water level.In an embodiment, gas generator of the present invention is placed in the water level in the first hollow bulb of water tank and/or electrolysis unit by water-level gauge detecting, to control whether supplementing of brine electrolysis, brine electrolysis is made to fill the water level of the first hollow bulb of water tank higher than 90% of full-water level.Therefore the design of gas generator of the present invention can avoid air cavity to be present in water tank, the temperature of electrolysis unit more can be made to reduce, thus reduce the risk of high temperature air blasting and improve its safety.
In addition, the first hollow bulb 20 of water tank 2 is further interconnected with pumping plant 5.Pumping plant 5 can be placed in the brine electrolysis W in the first hollow bulb 20 in order to forced circulation.The top 200 being positioned at the first hollow bulb 20 is circulate via intercommunicating pore 300 with the brine electrolysis of bottom 202.Wherein, when after electrolysis unit electrolysis brine electrolysis W, brine electrolysis W fills the water level of the first hollow bulb 20 of water tank 2 higher than 90% of full-water level.Further, the design of gas generator of the present invention is placed in the brine electrolysis in the first hollow bulb by forced circulation, make the air cavity in water tank level off to zero, to avoid pressure or the storage capacity of oxyhydrogen in water tank, causes air blasting.
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 controlling the quantum of output of hydrogen and oxygen gas mixture G in electrolysis unit 3.Wherein flow rate detector 82 optionally can cut off the electrical connection of electrolysis unit 3 and power supply (not being illustrated in figure).
In sum, the design that in the present invention, electrolysis unit is arranged at water tank can save space, the hydrogen and oxygen gas mixture of electrolysis unit generation is simultaneously by riddling the brine electrolysis of the first hollow bulb of water tank, air cavity can be avoided to be present in water tank, the temperature of electrolysis unit can also be made to reduce, thus prevent the generation of air blasting.Moreover the gas outlet of electrolysis unit and water inlet design in the present invention, make the brine electrolysis in water tank to be supplemented to electrolysis unit, and the hydrogen and oxygen gas mixture that electrolysis unit produces can be expelled to water tank, reach air water circulation.Further, in the present invention, the structural design that pumping plant, water tank and electrolysis unit are interconnected, can make the brine electrolysis be placed in the first hollow bulb carry out forced circulation, make the air cavity in water tank level off to zero, to prevent the generation of air blasting.
Refer to Figure 17.In the 4th specific embodiment, the present invention separately proposes a kind of gas generator, and it is a kind ofly have the gas generator that regulation and control brine electrolysis temperature and cooling produce effect of the brine electrolysis after hydrogen and oxygen gas mixture.In this enforcement, gas generator 1 comprises an electrolysis unit (not being illustrated in figure), pumping plant 5 and a chiller 7.Electrolysis unit 3 is equipped with a brine electrolysis W.Electrolysis unit 3 in order to electrolysis brine electrolysis W to produce a hydrogen and oxygen gas mixture G.Chiller 7 is connected to electrolysis unit 3, produces the brine electrolysis W after hydrogen and oxygen gas mixture G in order to cooling.Pumping plant 5 is connected between chiller 7 and electrolysis unit 3, in order to forced circulation brine electrolysis W.
Refer to Figure 17, Figure 17 illustrates the schematic diagram of gas generator of the present invention in the 5th specific embodiment.In the 5th specific embodiment, gas generator 1 of the present invention separately comprises a water tank 2.Water tank 2 has one first hollow bulb 20 and conduit 22 (being only represented by dotted lines in Figure 17).First hollow bulb 20 of water tank 2 is equipped with brine electrolysis W.Electrolysis unit 3 be arranged at water tank 2 the first hollow bulb 20 within, the first hollow bulb 20 is be interconnected with electrolysis unit 3.But not as limit, in another embodiment (as shown in Fig. 3 B, Fig. 5 B and Fig. 8), gas generator 1 of the present invention separately comprises a dividing plate 30.Dividing plate 30 comprises an intercommunicating pore 300.Dividing plate 30 is in order to be separated into top 200 and a bottom 202 by the first hollow bulb 20.Water tank 2 separately has an an outlet 249a and water inlet 249b.Top 200 and bottom 202 by intercommunicating pore to be interconnected.In this example, water hydrargyrum device 5 is between outlet 249a and water inlet 249b.Wherein the outlet 249a of water tank 2 is positioned at the top 200 of the first hollow bulb 20, and the water inlet 249b of water tank 2 is positioned at the bottom 202 of the first hollow bulb 10, is placed in brine electrolysis in top 200 and bottom 202 by water hydrargyrum device 5 to carry out forced circulation.In different embodiment, dividing plate 30 can be a part (as shown in fig. 4 a and fig. 4b) for electrolysis unit 3, can also be a part for water tank 2.
Further, in the 6th specific embodiment, gas generator 1 of the present invention separately comprises one atomization/volatilization gas mixing channel 4 (as shown in fig. 15).Atomization/volatilization gas mixing channel 4 can produce atomization gas G2 and mix with hydrogen and oxygen gas mixture G, sucks for this user to form health care gas.
First be described to the design of each element of the present invention respectively below.
First, because the structural design of water tank 2, electrolysis unit 3, pumping plant 5 and atomization/volatilization gas mixing channel 4 is in being described above, therefore do not repeat again at this.
Refer to Figure 15 A, Figure 15 B and Figure 17.In the 4th embodiment, chiller 7 of the present invention comprises radiator 70 and a fan 72.Radiator 70 comprises casing 700 and a radiating tube 702.Radiating tube 702 be distributed in radiator 70 casing 700 within.The shape of radiating tube 702 is a coil (not being illustrated in figure), and in order to increase integral heat sink area and then to improve radiating efficiency, but be not limited with this shape, when practical application, it can also be a spiral coil.In addition, when practical application, radiating tube 702 can by silver, aluminum, ferrum, copper, silver alloy, aluminium alloy, ferroalloy, the above material of copper alloy one made by.Further, radiator 70 comprises entrance 704 and an outlet 706.The entrance 704 of radiator 70 is casing 700 two surfaces relative to radiating tube 702 direction of this radiator 70 of connection, and the outlet 706 of radiator 70 is casing 700 two surfaces relative to radiating tube 702 direction of this radiator 70 of connection.Wherein, the entrance 704 of radiator 70 and outlet 706 are to be interconnected by radiating tube 702.
Further, in the 4th embodiment, gas generator 1 of the present invention separately comprises a microcomputer controller (not being illustrated in figure).Microcomputer controller is the temperature sensing brine electrolysis W, and according to the flow velocity that the temperature of sensed brine electrolysis W extracts to control pumping plant 5 and inputs.In addition, microcomputer controller comprises a temperature-sensitive sticker (not being illustrated in figure).Temperature-sensitive sticker is the temperature being placed in the brine electrolysis W in electrolysis unit 3 in order to sensing.In addition, microcomputer controller separately comprises a flow rate detector 82.Flow rate detector 82 in order to detect the flow of hydrogen and oxygen gas mixture G, and so as to controlling the quantum of output of hydrogen and oxygen gas mixture G in electrolysis unit 3.Flow rate detector 82 optionally can cut off the electrical connection (not being illustrated in figure) of electrolysis unit 3 and this power supply.
Above, after each design of each element is described, be described to the compound mode of each element and its application below.
In the water tank 2 assembled and electrolysis unit 3, for being arranged in the first hollow bulb 20 of water tank 2 by the electrolysis unit 3 after having assembled, wherein the first hollow bulb 20 of water tank 2 is be interconnected with electrolysis unit 3.In addition, because the compound mode of the water tank 2 assembled and electrolysis unit 3 is in being described above, therefore do not repeat again at this.
In the water tank 2 assembled, electrolysis unit 3, among pumping plant 5 and chiller 7, water tank 2 first hollow bulb 20 and electrolysis unit 3 are be interconnected (not being illustrated in figure), chiller 7 is connected to water tank 2, pumping plant 5 is connected between radiator 7 and water tank 2, but not as limit, when practical application, radiator 70 can be directly connected in electrolysis unit 3, pumping plant 5 can be directly connected between radiator 7 and water tank 2, meaning and gas generator of the present invention do not need water tank 2, or do not need electrolysis unit 3 to be arranged in water tank 2 can also complete gas generator of the present invention.
Then, the annexation between water tank 2, electrolysis unit 3, pumping plant 5 and chiller 7 that above-mentioned assembling completes further is described.Refer to Figure 15 A and Figure 15 B.The outlet 249a being provided with the water tank 2 of electrolysis unit 3 is interconnected with the entrance 704 of the radiator 70 of chiller 7, the outlet 706 of the radiator 70 of chiller 7 is interconnected with the oral siphon 50 of pumping plant 5, and the outlet pipe 52 of pumping plant 5 is interconnected with the water inlet 249b of water tank 2.But be not limited with above-mentioned annexation, when practical application, the outlet 249a being provided with the water tank 2 of electrolysis unit 3 can be interconnected with the oral siphon 50 of pumping plant 5, the outlet pipe 52 of pumping plant 5 can be interconnected with the entrance 704 of the radiator 70 of chiller 7, and the outlet 706 of the radiator 70 of chiller 7 can be interconnected with the water inlet 249b of water tank 2.
When practical application, water tank 2 is equipped with a brine electrolysis W, and electrolysis unit 3 is arranged in water tank 2, in order to electrolysis brine electrolysis W to produce a hydrogen and oxygen gas mixture G.The hydrogen and oxygen gas mixture G resulting from electrode runner S1 inputs to the first hollow bulb 20 via the upper perforation 360 of corresponding backing plate 36 and the first flow 370 of corresponding upper cover body 37.The hydrogen and oxygen gas mixture G inputing to the first hollow bulb 20 exports via the conduit 22 of water tank 2 further, and be available for users to suck, but not as limit, when practical application, the hydrogen and oxygen gas mixture G exported by the first hollow bulb 20 can further with via being atomized/atomization gas G2 that volatilization gas mixing channel 4 produces mixes, suck for user to form health care gas.
In addition, when electrolysis unit 3 suspends electrolysis brine electrolysis W to produce hydrogen and oxygen gas mixture G, conduit 22 can be used for supplementing input brine electrolysis W, is full of the first hollow bulb 20 and/or electrolysis unit 3 to make brine electrolysis W.Supplement the brine electrolysis W of input first hollow bulb 20 and can input to corresponding electrode runner S1 via the second runner 380 of the lower cover 38 of electrolysis unit 3 and multiple lower perforation 3202, brine electrolysis W required during to provide electrolysis unit 3 electrolysis.
In addition, water tank 2, electrolysis unit 3, pumping plant 5 and chiller 7 are interconnected.In time applying, produce the brine electrolysis W after hydrogen and oxygen gas mixture G forces to export to the radiator 70 of chiller 7 from the outlet 249a of water tank 2 entrance 704 by pumping plant 5, and cool in the radiating tube 702 of radiator 70.Cooled brine electrolysis W forces via the outlet 706 of radiator 70 oral siphon 50 exporting pumping plant 5 to by pumping plant 5, further, this brine electrolysis W forces via the outlet pipe 52 of pumping plant 5 the water inlet 249b inputing to water tank 2 by pumping plant 5.Therefore, gas generator of the present invention can produce the brine electrolysis after hydrogen and oxygen gas mixture by chiller cooling, and puts by force this brine electrolysis of circulation, to reach effect of heat radiation by pumping plant.Wherein, the temperature being placed in this brine electrolysis in this electrolysis unit is a conventional electrolysis temperature, and when practical application, the temperature being placed in the brine electrolysis W in electrolysis unit 3 can between 55 DEG C ~ 65 DEG C.
Further, microcomputer controller 8 is coupled to pumping plant 5 in order to sense the temperature of brine electrolysis W, and according to the flow velocity that the temperature of sensed brine electrolysis W extracts to control pumping plant 5 and inputs.When practical application, when the temperature of the brine electrolysis W sensed via temperature-sensitive sticker 80 is higher than a preset temperature, the too high information of this temperature can be passed back microcomputer controller 8, then microcomputer controller 8 can control the flow velocity that pumping plant 5 circulates to accelerate brine electrolysis W further, and the temperature of brine electrolysis is reduced to get back in preset temperature.On the contrary, when the temperature of the brine electrolysis W sensed via temperature-sensitive sticker 80 is lower than a preset temperature, the too low information of this temperature can be passed back microcomputer controller 8, then microcomputer controller 8 can control the flow velocity that pumping plant 5 circulates to slow down brine electrolysis W further, and the temperature of brine electrolysis is raised to get back in preset temperature.Wherein preset temperature is for providing the temperature of best electrolytic efficiency.In the present embodiment, preset temperature is a conventional electrolysis temperature.In practice, conventional electrolysis temperature is between 55 DEG C ~ 65 DEG C.
Comprehensive, of the present invention focusing on proposes a kind of gas generator, and it comprises electrolysis unit, chiller and pumping plant.Gas generator of the present invention can produce the brine electrolysis after hydrogen and oxygen gas mixture by chiller cooling, and puts by force cyclic electrolysis water by pumping plant, to reach effect of heat radiation.Meanwhile, the present invention's brine electrolysis temperature can be made to be positioned at temperature range that one provides best electrolytic efficiency, produces hydrogen and oxygen gas mixture to solve the problem consumed energy in order to electrolysis brine electrolysis effectively.
In addition, in an embodiment, water tank 2, electrolysis unit 3, pumping plant 5 and radiator 70 are interconnected.First hollow bulb 20 is separated into top 200 and a bottom 202 by dividing plate 30.In time applying, produce the brine electrolysis W after hydrogen and oxygen gas mixture G forces to export to radiator 70 from the outlet 249a on the top 200 being positioned at water tank 2 entrance 704 by pumping plant 5, and cool in radiator 70.Cooled brine electrolysis W forces via the outlet 706 of radiator 70 oral siphon 50 exporting pumping plant 5 to by pumping plant 5, further, this brine electrolysis W forces to input to the water inlet 249b being positioned at water tank 2 bottom 202 by the outlet pipe 52 of pumping plant 5 via pumping plant 5.Therefore, gas generator of the present invention can produce the brine electrolysis after hydrogen and oxygen gas mixture by radiator cooling, and puts by force circulation by pumping plant and be placed in brine electrolysis in the top of the first hollow bulb of water tank and bottom, to reach effect of heat radiation.
Refer to Fig. 9 A and Fig. 9 B.The present invention separately proposes a kind of gas generator, and it is a kind of gas generator with filtering function.In the 7th specific embodiment, gas generator 1 comprises electrolysis unit 3 and a condensate filter 6.The accommodating brine electrolysis W (not being illustrated in figure) of electrolysis unit 3.Electrolysis unit 3 in order to electrolysis brine electrolysis W to produce a hydrogen and oxygen gas mixture G.Condensate filter 6 connects electrolysis unit 3, in order to condensation hydrogen and oxygen gas mixture G and the impurity filtered in hydrogen and oxygen gas mixture G.Condensate filter 6 can be used for input supplementing water W2 (not being illustrated in figure) to electrolysis unit 3.In an embodiment, when electrolysis unit 3 suspends electrolysis brine electrolysis W to produce hydrogen and oxygen gas mixture G, condensate filter 6 can be used for inputting supplementing water W2, and impurity can be backwashed to electrolysis unit 3 via condensate filter 6 by supplementing water W2.
Further, in the 8th specific embodiment, gas generator 1 of the present invention separately comprises a water tank 2.Water tank 2 has one first hollow bulb 20.First hollow bulb 20 of water tank 2 is equipped with brine electrolysis W.Electrolysis unit 3 be arranged at water tank 2 the first hollow bulb 20 within.
Further, in the 9th specific embodiment, gas generator 1 of the present invention separately comprises one atomization/volatilization gas mixing channel 4 (as shown in fig. 15).Atomization/volatilization gas mixing channel 4 can be connected with condensate filter 6, in order to the hydrogen and oxygen gas mixture G after receiving filtration.Hydrogen and oxygen gas mixture G after atomization/volatilization gas mixing channel 4 can produce atomization gas G2 and filter mixes, and sucks for this user to form health care gas.
Referring to Fig. 9 A and Fig. 9 B, Fig. 9 A and Fig. 9 B is the schematic diagram illustrating the different visual angles of gas generator of the present invention in the tenth specific embodiment.In the tenth specific embodiment, gas generator 1 of the present invention separately can comprise a pumping plant 5 and chiller 7.
First be described to the design of each element of the present invention respectively below.
First, because the structural design of water tank 2, electrolysis unit 3 and atomization/volatilization gas mixing channel 4 is in being described above, therefore do not repeat again at this.
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 present invention has blowhole 60 and a venthole 62.Blowhole 60 can be connected to electrolysis unit 3, in order to receive hydrogen and oxygen gas mixture.Venthole 62 is in order to discharge the hydrogen and oxygen gas mixture G after filtering.In addition, condensate filter 6 of the present invention includes multiple condensate film 64.Each condensate film 64 has a runner 640a, and the runner 640a of the condensate film 64 and runner 640a of adjacent condensate film 64 is interconnected, so as to forming the circulatory flow 640 for hydrogen and oxygen gas mixture G circulation, in order to condensation hydrogen and oxygen gas mixture G.Blowhole 60 and venthole 62 are interconnected by circulatory flow 640.In an embodiment, the runner 640a of condensate film 64 is formed by a gradual-enlargement type runner 642 is communicated with runner 644 with one.As shown in Figure 14B, gradual-enlargement type runner 642 is the runner of a cross section flaring, but is not limited with the gradual-enlargement type runner 642 shown in Figure 14 B, and when practical application, the cross section of gradual-enlargement type runner can be semi-circular, triangular form or trapezoidal.Gradual-enlargement type runner 642 has relatively wide one end and relatively narrow one end.Relatively wide one end and relatively narrow one end of gradual-enlargement type runner 642 all have an opening.Be communicated with runner 644 and there are a runner and two corresponding openings.The opening being communicated with two of runner 644 corresponding is interconnected by runner.When gradual-enlargement type runner 642 be communicated with runner 644 be interconnected time, gradual-enlargement type runner 642 with connection runner 644 can be interconnected with the connection of the opening being communicated with runner 644 by the opening of relative wide one end of gradual-enlargement type runner 642.The structural design of the runner 640a of condensate film 64, it makes horizontal run (i.e. gradual-enlargement type runner 642) be interconnected with vertical run (being namely communicated with runner 644), but horizontal run is not limited with the runner of cross section flaring, when practical application, horizontal run can also be the equal runner in cross section.Further, when the runner 640a of the condensate film 64 and runner 640a of adjacent condensate film 64 is interconnected, the runner 640a of condensate film 64 is interconnected with the connection being communicated with the opening of runner 644 of adjacent condensate film 64 by the opening of relative narrow one end of the gradual-enlargement type runner 642 of condensate film 64 with the runner 640a of adjacent condensate film 64.Therefore, the structural design of the runner 640a of condensate film 64, it makes the runner 640a of the condensate film 64 and runner 640a of adjacent condensate film 64 be interconnected, so as to forming the circulatory flow 640 for hydrogen and oxygen gas mixture circulation.Meaning is namely in the present embodiment, and the connected mode of condensate film and adjacent condensate film, can order about hydrogen and oxygen gas mixture by longer condensation and filtration path, and then reach better condensation and filter effect.Further, in an embodiment, in runner 640a, an activated carbon fiber can be provided with, in order to filter the impurity in hydrogen and oxygen gas mixture G.Runner 640a separately can be provided with arbitrary filtering material be made up of pottery, quartz, kieselguhr, meerschaum or more, and filtering material further can filter the impurity in hydrogen and oxygen gas mixture G.Wherein impurity is the electrolyte in brine electrolysis W, and it is sodium hydroxide.But not as limit, when practical application, impurity can be calcium carbonate, sodium chloride etc.In addition, in an embodiment, blowhole 60 of the present invention can be made up of a drainage screen 600 and a filtration square 602.Drainage screen 600 and filtration square 602 can be connected to electrolysis unit 3, in order to receive hydrogen and oxygen gas mixture G, and preliminarily filter hydrogen and oxygen gas mixture G.Wherein electrolysis unit 3 is placed in water tank 2 in order to be connected with condensate filter 6 further.
Above, after each design of each element is described, be described to the compound mode of each element and its application below.
In the electrolysis unit 3 assembled, multiple electrode 34 is arranged at intervals at cell body 32 respectively, backing plate 36 is arranged at the upper surface of each electrode 34, upper cover body 37 is covered on the other end of backing plate 36 relative to cell body 32, and lower cover 38 is covered on the other end of lower surface relative to upper cover body 37 of cell body 32.
In the water tank 2 assembled and electrolysis unit 3, the anode strip 342 of the electrolysis unit 3 after having assembled and cathode sheets 340 are locked on water tank lid 26 separately by two electrode columns 33.And checkout gear (as flow rate detector 82) by through water tank lid 26 multiple cap bore 261 and be arranged on water tank lid 26.Sealing gasket 28 is arranged at water tank cell body 24, and is mutually fitted together to by the 3rd embedded structure 282 of sealing gasket 28 and the first embedded structure 246 of water tank cell body 24.First lateral margin 248 of water tank cell body 24 is covered in the second hollow bulb 264 of water tank lid 26 by the second peristome 266 of water tank lid 26, water tank cell body 24 and water tank lid 26 to be combined closely, and is fixedly arranged on vacantly in water tank 2 by electrolysis unit 3.Wherein, water tank 2 and electrolysis unit 3 are interconnected.
In the water tank 2 assembled, electrolysis unit 3 and condensate filter 6, the water tank 2 and the condensate filter 6 that are provided with electrolysis unit 3 are to be interconnected by the connection between the conduit 22 of water tank 2 and the blowhole 60 of condensate filter 6.Further, atomization/volatilization gas mixing channel 4 can be connected to the venthole 62 of condensate filter 6.
When practical application, water tank 2 is equipped with a brine electrolysis W, and electrolysis unit 3 is arranged in water tank 2, in order to electrolysis brine electrolysis W to produce a hydrogen and oxygen gas mixture G.The hydrogen and oxygen gas mixture G resulting from electrode runner S1 inputs to the first hollow bulb 20 via the upper perforation 360 of corresponding backing plate 36 and the first flow 370 of corresponding upper cover body 37.The hydrogen and oxygen gas mixture G inputing to the first hollow bulb 20 exports via the conduit 22 of water tank 2 further.The hydrogen and oxygen gas mixture G exported by the conduit 22 of water tank 2 can enter condensate filter 6 via the blowhole 60 of condensate filter 6 and carry out condensation and filtration.First the hydrogen and oxygen gas mixture G entering the blowhole 60 of condensate filter 6 can first preliminarily be filtered by drainage screen 600 and filtration square 602.Then, hydrogen and oxygen gas mixture G after preliminarily filtering can enter circulatory flow 640 further and carry out condensation, meanwhile, hydrogen and oxygen gas mixture G is by being arranged at activated carbon fiber in runner 640a and filtering material and carrying out filtering and being adsorbed in by impurity in circulatory flow in 640.Then, hydrogen and oxygen gas mixture G after filtration is by the hydrogen and oxygen gas mixture G after venthole 62 output filtering of condensate filter 6, and be available for users to suck, but not as limit, when practical application, hydrogen and oxygen gas mixture G after the filtration exported by condensate filter 6 can further with via being atomized/atomization gas G2 that volatilization gas mixing channel 4 produces mixes, suck for user to form health care gas.
In addition, in an embodiment, when electrolysis unit 3 suspends electrolysis brine electrolysis W to produce hydrogen and oxygen gas mixture G, the venthole 62 of condensate filter 6 can be used for input with supplementary supplementing water W2.The supplementing water W2 supplemented by the venthole 62 of condensate filter 6 can input in the first hollow bulb 20 of water tank 2 via the conduit 22 be connected with venthole 62.Supplement the brine electrolysis W of input first hollow bulb 20 and can input to corresponding electrode runner S1 via the second runner 380 of the lower cover 38 of electrolysis unit 3 and multiple lower perforation 3202, brine electrolysis W required during to provide electrolysis unit 3 electrolysis.And the impurity be adsorbed in the circulatory flow 640 of condensate filter 6 can also be backwashed in the water tank 2 being provided with electrolysis unit 3 via blowhole 60 and conduit 22 by above-mentioned supplementing water W2.
In addition, in an embodiment, the flow rate detector 82 coupling electrolysis unit 3 can detect the flow of hydrogen and oxygen gas mixture G.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..
Comprehensive, of the present invention focusing on proposes a kind of gas generator, and it comprises electrolysis unit and condensate filter.In gas generator of the present invention, the impurity that the hydrogen and oxygen gas mixture that electrolysis unit produces can be carried out condensation by condensate filter and be filtered wherein, with the hydrogen and oxygen gas mixture providing an applicable human body to suck.Meanwhile, can while supplementing water, electrolyte be backwashed to electrolysis unit by design of the present invention, in order to reduce electrolytical consumption and to avoid electrolyte to block in condensate filter.
Refer to Figure 15 A, Figure 15 B and Figure 16.In the 11 specific embodiment, the present invention separately proposes a kind of gas generator, and it is a kind of gas generator having humidification function.Gas generator 1 comprises an electrolysis unit 3 (not being illustrated in figure) and a humidification device 9.Electrolysis unit 3 is equipped with brine electrolysis W, in order to electrolysis brine electrolysis W to produce a hydrogen and oxygen gas mixture G.Humidification device 9 connects electrolysis unit 3, in order to receive and humidified hydrogen oxygen gas mixture G.
Further, in the 12 specific embodiment, gas generator 1 of the present invention separately comprises a condensate filter 6.Condensate filter 6 can be located between electrolysis unit 3 and humidification device 9, the hydrogen and oxygen gas mixture G produced in order to condensation electrolysis unit 3 impurity filtered in hydrogen and oxygen gas mixture G.Humidification device 9 is in order to receive the hydrogen and oxygen gas mixture after also humidifying filtration.
Further, in the 13 specific embodiment, gas generator 1 of the present invention separately comprises one atomization/volatilization gas mixing channel 4.Atomization/volatilization gas mixing channel 4 can be connected to the humidification device be connected with condensate filter, in order to the hydrogen and oxygen gas mixture G after receiving filtration and humidifying.Atomization/volatilization gas mixing channel 4 can produce atomization gas G2 and mix with the hydrogen and oxygen gas mixture G after filtration and humidifying, sucks for user to form health care gas.But not as limit, in another embodiment, atomization/volatilization gas mixing channel 4 can be connected to humidification device, in order to receive the hydrogen and oxygen gas mixture G after humidifying.Atomization/volatilization gas mixing channel 4 can produce atomization gas G2 and mix with the hydrogen and oxygen gas mixture G after humidifying, sucks for user to form health care gas.But not as limit, in an embodiment, atomization of the present invention/volatilization gas mixing channel 4 can be a hand-held atomising device (not being illustrated in figure).Hand-hold atomization device can connect humidification device 9, in order to receive the hydrogen and oxygen gas mixture after humidifying.Hand-hold atomization device produces an atomization gas and mixes with the hydrogen and oxygen gas mixture after humidifying, sucks for user to form health care gas.But not as limit, in another embodiment, hand-hold atomization device can connect the humidification device be connected with condensate filter, in order to the hydrogen and oxygen gas mixture after receiving filtration and humidifying.Hand-hold atomization device produces atomization gas and mixes with the hydrogen and oxygen gas mixture after filtration and humidifying, sucks for user to form health care gas.When practical application, hand-hold atomization device is for having a pressing type structure, and the aequum that namely user can export health care gas through the pressing type structure pressing hand-hold atomization device sucks.Wherein atomization gas can be selected from the one in the group be made up of water vapour, atomization liquid medicine, volatile spirits and combination thereof.
Referring to Figure 15 A and Figure 15 B, Figure 15 A and Figure 15 B is the schematic diagram illustrating the different visual angles of gas generator of the present invention in the 14 specific embodiment.Further, in the 14 specific embodiment, gas generator 1 of the present invention separately comprises water tank 2, water hydrargyrum device 5, chiller 7, gas output device 10.Wherein gas output device 10 can suck for user in order to export health care gas, and health care gas is hydrogen and oxygen gas mixture G after humidifying and the mixing of atomization gas G2.
First be described to the design of each element of the present invention respectively below.
First, because the structural design of condensate filter 6 and atomization/volatilization gas mixing channel 4 is in being described above, therefore do not repeat again at this.
Humidification device 9 of the present invention includes hollow body 90,1 second conduit 92, at least one outlet tube 94, rocking equipment 95 (being only represented by dotted lines in Figure 15 A and Figure 15 B), one the 3rd conduit 96 and one the 4th conduit 98.Hollow body 90 can in order to an accommodating supplementing water W2.Second conduit 92 is arranged at can in order to be connected with electrolysis unit 3 (not being illustrated in figure) on hollow body 90.At least one outlet tube 94 to be arranged among hollow body 90 and to be connected with the second conduit 92.Second conduit 92 is connected to form a T-type structure with two outlet tubes 94, but not as limit, when practical application, visual service condition adjusts the connection between the second conduit and at least one outlet tube 94.Further, the surface of two outlet tubes 94 all has multiple perforation.In an embodiment, it is in the scope of 2 nanometer to 10 nanometers that perforation can have nano level aperture, in order to carry out refinement to gas to form diffluent bubble disintegration, but not as limit, when practical application, the visual user demand of pore size of perforation adjusts.The end connecting two outlet tubes 94 of the second conduit 92 is all respectively arranged with a rubber stopper, hollow body 90 is expelled to by multiple nanometers perforation (not being illustrated in figure) of two outlet tubes 94 in order to make the hydrogen and oxygen gas mixture G received by the second conduit 92, but not as limit, when practical application, the end connecting two outlet tubes 94 of the second conduit 92 also can be closed design.In an embodiment, rocking equipment 95 can be arranged among hollow body 90 and to be positioned at the below of at least one outlet tube 94, in order to shake supplementing water.Rocking equipment 95 can comprise a sonicator, is used for shaking the supplementing water in hollow body 90.In practice, rocking equipment is not limited only to the sonicator of this specific embodiment, its position is also not limited to the position shown in Figure 15 B, anyly to be arranged on hollow body and water to be shaken or stir with the device effectively disperseing hydrogen and oxygen gas mixture to become micro-bubble, all belonging to the rocking equipment that the present invention defines.Such as, rocking equipment 95 also can comprise centrifugeblade and connect the CD-ROM drive motor of centrifugeblade, and CD-ROM drive motor can drive centrifugeblade to rotate and produce eddy current with Yu Shuizhong, and the hydrogen in auxiliary hydrogen and oxygen gas mixture is more effectively scattered in water and forms hydrogen water.Rocking equipment 95 also can comprise above-mentioned sonicator, centrifugeblade and CD-ROM drive motor, makes the generation more effective percentage of hydrogen water.3rd conduit 96 can be arranged on hollow body 90, in order to export hydrogen water H or in order to supplementary input supplementing water W2.When practical application, the 3rd conduit can be communicated with a guide hole, by the 3rd conduit by guide hole to pour out hydrogen water H or to pour supplementing water W2 into.4th conduit 98 can be arranged on hollow body 90, in order to export the hydrogen and oxygen gas mixture G after humidifying.
Further, in another example, gas generator 1 of the present invention separately comprises a water tank 2.Water tank 2 has one first hollow bulb 20.First hollow bulb 20 of water tank 2 is equipped with brine electrolysis W.Electrolysis unit 3 be arranged at water tank 2 the first hollow bulb 20 within.In addition, humidification device 9 of the present invention separately can comprise one second water hydrargyrum device (not being illustrated in figure).Second water hydrargyrum device can be arranged on water tank lid 26 and to be communicated in the first hollow bulb 20, inner produces a negative pressure in order to the gas that extracts water tank 2 inside to make it.
Above, after each design of each element is described, be described to the compound mode of each element and its application below.
In an electrolysis unit assembled 3, multiple electrode 34 is arranged at intervals at cell body 32 respectively, backing plate 36 is arranged at the upper surface of each electrode 34, upper cover body 37 is covered on the other end of backing plate 36 relative to cell body 32, and lower cover 38 is covered on the other end of lower surface relative to upper cover body 37 of cell body 32.
In the water tank 2 assembled and electrolysis unit 3, the anode strip 342 of the electrolysis unit 3 after having assembled and cathode sheets 340 are locked on water tank lid 26 separately by two electrode columns 33.And checkout gear (as flow rate detector 82) by through water tank lid 26 multiple cap bore 261 and be arranged on water tank lid 26.Sealing gasket 28 is arranged at water tank cell body 24, and is mutually fitted together to by the 3rd embedded structure 282 of sealing gasket 28 and the first embedded structure 246 of water tank cell body 24.First lateral margin 248 of water tank cell body 24 is covered in the second hollow bulb 264 of water tank lid 26 by the second peristome 266 of water tank lid 26, water tank cell body 24 and water tank lid 26 to be combined closely, and is fixedly arranged on vacantly in water tank 2 by electrolysis unit 3.Wherein, water tank 2 and electrolysis unit 3 are interconnected.
In the water tank 2 assembled, electrolysis unit 3, condensate filter 6 and humidification device 9, the water tank 2 and the condensate filter 6 that are provided with electrolysis unit 3 are to be interconnected by the connection between the conduit 22 of water tank 2 and the blowhole 60 of condensate filter 6.Then, and the condensate filter 6 that is interconnected of water tank and humidification device 9 be to be interconnected by the connection between the venthole 60 of condensate filter 6 and the second conduit 92 of humidification device 9.Further, in the 13 specific embodiment, atomization/volatilization gas mixing channel 4 can be connected to the 4th conduit 98 of humidification device 9.
When practical application, water tank 2 is equipped with a brine electrolysis W, and electrolysis unit 3 is arranged in water tank 2, in order to electrolysis brine electrolysis W to produce a hydrogen and oxygen gas mixture G.The hydrogen and oxygen gas mixture G resulting from electrode runner S1 inputs to the first hollow bulb 20 via the upper perforation 360 of corresponding backing plate 36 and the first flow 370 of corresponding upper cover body 37.The hydrogen and oxygen gas mixture G inputing to the first hollow bulb 20 exports via the conduit 22 of water tank 2 further.The hydrogen and oxygen gas mixture G exported by the conduit 22 of water tank 2 can enter condensate filter 6 via the blowhole 60 of condensate filter 6 and carry out condensation and filtration.First the hydrogen and oxygen gas mixture G entering the blowhole 60 of condensate filter 6 can first preliminarily be filtered by drainage screen 600 and filtration square 602.Then, hydrogen and oxygen gas mixture G after preliminarily filtering can enter circulatory flow 640 further and carry out condensation, meanwhile, hydrogen and oxygen gas mixture G is by being arranged at activated carbon fiber in runner 640a and filtering material and carrying out filtering and being adsorbed in by impurity in circulatory flow in 640.Then, the hydrogen and oxygen gas mixture G after filtration is by the hydrogen and oxygen gas mixture G after venthole 62 output filtering of condensate filter 6.
Moreover the hydrogen and oxygen gas mixture G after filtration inputs to humidification device 9 by the second conduit 92 be connected with venthole 62.Hydrogen and oxygen gas mixture G after the filtration received by the second conduit 92 bores a hole by multiple nanometers of two outlet tubes 94 to be expelled in hollow body 90.When practical application, multiple nanometer perforation that the surface due to outlet tube 94 has, it can be used for carrying out refinement, to form diffluent bubble disintegration to the hydrogen and oxygen gas mixture of input humidification device.Meanwhile, the supplementing water be placed in humidification device 9 is shaken by rocking equipment 95, can easily be dissolved in the supplementing water after concussion in order to make gas.Wherein the above-mentioned hydrogen and oxygen gas mixture G boring a hole discharged by nanometer carries out humidifying to produce the hydrogen and oxygen gas mixture after humidifying by the supplementing water after rocking equipment 95 shakes, and be available for users to suck, but not as limit, when practical application, hydrogen and oxygen gas mixture G after the humidifying exported by humidification device 9 can further with via being atomized/atomization gas G2 that volatilization gas mixing channel 4 produces mixes, suck for user to form health care gas.In addition, the hydrogen and oxygen gas mixture G that the above-mentioned outlet tube having nanometer perforation by surface is discharged also can the supplementing water after shaking via rocking equipment 95 be combined to produce a hydrogen water H.More particularly, the hydrogen and oxygen gas mixture G that the outlet tube having nanometer perforation by surface is discharged is diffluent bubble disintegration, and the supplementing water after shaking via rocking equipment 95 is easily make gas dissolving in supplementing water wherein.Therefore the hydrogen water H dissolving higher concentration hydrogen-oxygen can be produced through hydrogen or oxygen gas generator of the present invention.
In addition, in another embodiment, the hydrogen and oxygen gas mixture produced via electrolysis unit 3 electrolysis brine electrolysis W directly can enter humidification device 9 and carry out humidifying.The hydrogen and oxygen gas mixture that namely meaning results from electrode runner S1 inputs to the first hollow bulb 20 via the upper perforation 360 of corresponding backing plate 36 and the first flow 370 of corresponding upper cover body 37.The hydrogen and oxygen gas mixture inputing to the first hollow bulb 20 exports via the conduit 22 of water tank 2 further.The hydrogen and oxygen gas mixture exported by the conduit 22 of water tank 2 can input to humidification device 9 to produce the hydrogen and oxygen gas mixture after humidifying through the second conduit 92 be connected with conduit 22, and is available for users to suck.But not as limit, when practical application, the hydrogen and oxygen mixture physical ability after the humidifying exported by humidification device 9 further with via being atomized/atomization gas that volatilization gas mixing channel 4 produces mixes, suck for user to form health care gas.In addition, the hydrogen and oxygen gas mixture G that the above-mentioned outlet tube having nanometer perforation by surface is discharged also can the supplementing water after shaking via rocking equipment 95 be combined to produce a hydrogen water.
In addition, when electrolysis unit 3 suspends electrolysis brine electrolysis to produce hydrogen and oxygen gas mixture, the second water hydrargyrum device can in order to extract the gas of water tank 2 inside to make its inner generation negative pressure.The supplementing water W2 supplementing input via the 3rd conduit 96 to be inputted back by humidification device 9 by above-mentioned negative pressure and is provided with in the water tank 2 of electrolysis unit 3.More particularly, supplementing water can input to condensate filter 6 by humidification device 9 by the connection between the second conduit 92 of humidification device 9 and the venthole 62 of condensate filter 6.Further, the impurity be adsorbed in the circulatory flow 640 of condensate filter 6 can backwash in the water tank 2 being provided with electrolysis unit 3 via blowhole 60 and conduit 22 by above-mentioned supplementing water, in order to recover circulatory flow filter capacity, prevent the obstruction of circulatory flow and corrosion and lower electrolytical consumption.In practice, the present invention utilizes supplementing water to backwash in the water tank 2 being provided with electrolysis unit 3 by impurity (meaning and electrolyte), and it can in order to the brine electrolysis providing electrolysis unit 3 to carry out needed for electrolysis.Further, the brine electrolysis W of the first hollow bulb 20 supplementing input water tank 2 can input to corresponding electrode runner S1 via the second runner 380 of the lower cover 38 of electrolysis unit 3 and multiple lower perforation 3202, brine electrolysis W required during to provide electrolysis unit 3 electrolysis.
Comprehensive, of the present invention focusing on proposes a kind of gas generator, and it comprises electrolysis unit and humidification device.In gas generator of the present invention, the hydrogen and oxygen gas mixture that electrolysis unit produces can carry out humidifying by humidification device, with the hydrogen and oxygen gas mixture providing applicable human body to suck.In addition, the hydrogen and oxygen gas mixture that electrolysis unit produces can pass through humidification device, to produce the hydrogen water of the hydrogen and oxygen gas mixture dissolving higher concentration, when practical application, visual user is required to produce the hydrogen water with the hydrogen and oxygen gas mixture of desired concn.In addition, can, in order to supplementary supplementing water, electrolyte be backwashed to electrolysis unit by design of the present invention simultaneously, in order to recover circulatory flow filter capacity, prevent the obstruction of circulatory flow and corrosion and lower electrolytical consumption.
Finally, refer to Figure 18 A, Figure 18 B, Figure 19, Figure 20 A and Figure 20 B, Figure 18 A and Figure 18 B is the schematic diagram illustrating the different visual angles of gas generator of the present invention in the 15 specific embodiment, Figure 19 illustrates the rearview of gas generator of the present invention in embodiment shown in Figure 18 A, and Figure 20 A and Figure 20 B illustrates the top view only in Figure 18 A illustrated embodiment with condensate filter and water tank lid and cuts open along the D-D line of this top view the profile established.In the 15 specific embodiment, gas generator of the present invention comprises water tank, electrolysis unit, atomization/volatilization gas mixing channel, pumping plant, condensate filter, chiller and humidification device.Because the structural design of said elements is in being described above, therefore do not repeat again at this.Further, compared to the circulatory flow shown in Figure 14 B, in the present embodiment (Figure 20 B), circulatory flow 640 by means of only two groups of runner 640a form the effect that can reach condensation, the design simplification of condensate filter 6 and cost can be made to reduce simultaneously.In addition, in the present embodiment, pumping plant 5 (not being illustrated in figure), condensate filter 6 and chiller 7 are all integrated and are arranged on the lid of water tank 2, make it become a modular design, and its design compared to the 14 specific embodiment simultaneously can save space more.In addition, when modular water tank 2, pumping plant 5, condensate filter 6 and chiller 7 is assembled with atomization/volatilization gas mixing channel 4 and humidification device 9, the present invention can have advantage that is easy to assembly and pipeline simplification, more optimizes to make the global design of gas generator of the present invention.
In an embodiment, when electrolysis unit is electrically connected with external power source, the output voltage of power supply is about between 17 volts (V) to 27 volts (V), the output current of power supply is about between 30 amperes (A) to 40 amperes (A), and namely electrolysis unit about produces the gas output between 1.5 liters to 4.0 liters per minute.In time using, the voltage about 1.5 volts (V) of each group electrode (between both positive and negative polarity) is between 3 volts (V), if any eight groups of voltages then used between 12V ~ 24V.But not as limit, when practical application, when electrolysis unit is electrically connected with external power source, the output voltage of power supply is about between 5 volts (V) to 24 volts (V), the output current of power supply is about between 2 amperes (A) to 150 amperes (A), namely the power of electrolysis unit is about between 10 watts (i.e. about 5V*2A) to 3600 watts (i.e. about 24V*150A), and electrolysis unit can produce the gas output between 0.01 liter to 12 liters per minute.
Further, the present invention proposes a kind of gas generator, and it comprises electrolysis unit and humidification device.In gas generator of the present invention, the hydrogen and oxygen gas mixture that electrolysis unit produces can carry out humidifying by humidification device, with the hydrogen and oxygen gas mixture providing applicable human body to suck.In addition, the hydrogen and oxygen gas mixture that electrolysis unit produces can pass through humidification device, to produce the hydrogen water of the hydrogen and oxygen gas mixture dissolving higher concentration, when practical application, visual user is required to produce the hydrogen water with the hydrogen and oxygen gas mixture of desired concn.In addition, can, in order to supplementary supplementing water, electrolyte be backwashed to electrolysis unit by design of the present invention simultaneously, in order to recover circulatory flow filter capacity, prevent the obstruction of circulatory flow and corrosion and lower electrolytical consumption.
By the above detailed description of preferred embodiments, be wish clearly to describe feature of the present invention and spirit, and not with above-mentioned disclosed preferred embodiment, category of the present invention limited.On the contrary, its objective is wish to contain various change and tool equality be arranged in the present invention institute in the category of the scope of the claims applied for.Although the present invention discloses as above with embodiment; so itself and be not used to limit the present invention; anyly be familiar with this those skilled in the art; without departing from the spirit and scope of the present invention; when being used for a variety of modifications and variations, the scope that therefore protection scope of the present invention ought define depending on appending claims is as the criterion.
Claims (15)
1. a gas generator, is characterized in that, comprises:
One electrolysis unit, is equipped with a brine electrolysis, in order to this brine electrolysis of electrolysis to produce a hydrogen and oxygen gas mixture; And
One humidification device, include a hollow body, one second conduit and at least one outlet tube, this hollow body is in order to an accommodating supplementing water, this second conduit is in order to receive this hydrogen and oxygen gas mixture, described at least one outlet tube and this second tubes connection, the surface of described at least one outlet tube has multiple perforation;
Wherein when this this brine electrolysis of electrolysis unit electrolysis is to produce this hydrogen and oxygen gas mixture, this hydrogen and oxygen gas mixture is discharged via described multiple perforation of described at least one outlet tube, with this hydrogen and oxygen gas mixture of humidifying.
2. gas generator according to claim 1, it is characterized in that, this humidification device separately comprises a rocking equipment, this rocking equipment is in order to shake this supplementing water, this supplementing water after the concussion of this rocking equipment is in order to this hydrogen and oxygen gas mixture of humidifying, and this supplementing water after this hydrogen and oxygen gas mixture can shake with this rocking equipment is combined and produces a hydrogen water.
3. gas generator according to claim 2, is characterized in that, this humidification device separately includes one the 3rd conduit, and the 3rd conduit is arranged on this hollow body, in order to export this hydrogen water.
4. gas generator according to claim 3, it is characterized in that, when this electrolysis unit suspends this brine electrolysis of electrolysis to produce this hydrogen and oxygen gas mixture, this humidification device can supplement this supplementing water, and via the 3rd conduit of this humidification device to input this supplementing water in this hollow body of this humidification device.
5. gas generator according to claim 1, is characterized in that, this humidification device separately includes one the 4th conduit, and the 4th conduit is arranged on this hollow body, in order to export this hydrogen and oxygen gas mixture after humidifying.
6. gas generator according to claim 5, it is characterized in that, separately comprise one atomization/volatilization gas mixing channel, wherein this atomization/volatilization gas mixing channel connects the 4th conduit of this humidification device, in order to receive this hydrogen and oxygen gas mixture after humidifying, wherein this atomization/volatilization gas mixing channel produces an atomization gas and mixes with this hydrogen and oxygen gas mixture after humidifying, suck for a user to form a health care gas, wherein this atomization gas is selected from the one in the group be made up of water vapour, atomization liquid medicine, volatile spirits and combination thereof.
7. gas generator according to claim 5, it is characterized in that, separately comprise a hand-held atomising device, wherein this hand-hold atomization device connects the 4th conduit of this humidification device, in order to receive this hydrogen and oxygen gas mixture after humidifying, wherein this hand-hold atomization device produces an atomization gas and mixes with this hydrogen and oxygen gas mixture after humidifying, suck for a user to form a health care gas, wherein this atomization gas is selected from the one in the group be made up of water vapour, atomization liquid medicine, volatile spirits and combination thereof.
8. gas generator according to claim 1, is characterized in that, separately includes:
One condensate filter, be located between this electrolysis unit and this humidification device, this hydrogen and oxygen gas mixture produced in order to this electrolysis unit of condensation the impurity filtered in this hydrogen and oxygen gas mixture, this condensate filter has a blowhole and a venthole, this blowhole is connected to this electrolysis unit, in order to receive this hydrogen and oxygen gas mixture, this venthole is in order to discharge this hydrogen and oxygen gas mixture after filtering;
Wherein this second tubes connection of this humidification device is in this venthole of this condensate filter, in order to this hydrogen and oxygen gas mixture after receiving filtration.
9. gas generator according to claim 8, it is characterized in that, when this electrolysis unit suspends this brine electrolysis of electrolysis to produce this hydrogen and oxygen gas mixture, this humidification device can supplement this supplementing water, and via this second conduit of this humidification device and this venthole of this condensate filter to input this supplementing water, this impurity can also be backwashed to this electrolysis unit by this supplementing water this blowhole via this condensate filter.
10. gas generator according to claim 1, is characterized in that, the generation flow rate of this hydrogen and oxygen gas mixture of this gas generator is between 0.01L/min. and 12L/min..
11. gas generators according to claim 1, it is characterized in that, this electrolysis unit comprises multiple electrode, described multiple electrode package contains a cathode sheets, an anode strip and multiple bipolar electrode sheet, described multiple bipolar electrode sheet is arranged at intervals between this cathode sheets and this anode strip, this cathode sheets is connected to the negative pole of a power supply, and this anode strip is connected to the positive pole of this power supply.
12. gas generators according to claim 11, is characterized in that, the voltage difference of the one group of electrolysis electrode be made up of two adjacent these bipolar electrode sheets is between 1.5V ~ 3V.
13. gas generators according to claim 1, is characterized in that, the aperture of this perforation is between the scope of 2 nanometer to 10 nanometers.
14. gas generators according to claim 2, is characterized in that, this rocking equipment comprises a sonicator to shake this supplementing water.
15. gas generators according to claim 2, it is characterized in that, this rocking equipment comprises a centrifugeblade and connects a CD-ROM drive motor of this centrifugeblade, and this CD-ROM drive motor drives this centrifugeblade to rotate to shake this supplementing water and centrifugal.
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| TW103135891A TW201615894A (en) | 2014-10-16 | 2014-10-16 | A gas generator |
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| CN107401794A (en) * | 2016-05-19 | 2017-11-28 | 水素村营农组合法人 | Humidifier |
| CN108624903A (en) * | 2017-08-25 | 2018-10-09 | 林信涌 | Electrolytic water device |
| CN110681176A (en) * | 2019-11-07 | 2020-01-14 | 北京中电丰业技术开发有限公司 | Electric heating type gas-liquid separator |
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| TW201615894A (en) | 2016-05-01 |
| CN109364345B (en) | 2021-09-28 |
| CN109364345A (en) | 2019-02-22 |
| CN105498065B (en) | 2018-09-11 |
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