CN105617503A

CN105617503A - Gas generator

Info

Publication number: CN105617503A
Application number: CN201410619929.2A
Authority: CN
Inventors: 林信湧
Original assignee: Individual
Current assignee: Shanghai Medical Science And Technology Co Ltd
Priority date: 2014-10-16
Filing date: 2014-11-05
Publication date: 2016-06-01
Anticipated expiration: 2034-11-05
Also published as: CN105617503B; TWI570275B; TW201615895A

Abstract

The invention discloses a gas generator, which comprises an electrolysis device and a condensation filter. The electrolysis device is used for electrolyzing the electrolyzed water to generate hydrogen-oxygen mixed gas. The condensation filter is used for condensing the hydrogen-oxygen mixed gas and filtering impurities in the hydrogen-oxygen mixed gas. The condensing filter has an air inlet and an air outlet. When the air outlet of the condensation filter is used for inputting supplementary water to the electrolysis device. Therefore, the gas generator of the invention can provide hydrogen-oxygen mixed gas suitable for human body to inhale, can also reduce the consumption of electrolyte and avoid the electrolyte from being blocked in the condensation filter.

Description

Gas generator

Technical field

The invention relates to a kind of gas generator, in particular to a kind of gas generator with filtering function.

Background technology

All the time, the mankind are pay attention to completely for life, the exploitation of the technology of many medical treatment, are all used to anti-disease, to continue the life of the mankind. The medical mode major part in past is all belonging to passively, namely when disease occurs, then suits the medicine to the illness and carries out medical treatment, such as operation, administration, even the taking good care of of the chemotherapy of cancer, radiation treatment or chronic disease, rehabilitation, rectification etc. But in recent years, many medical experts are increasingly towards preventative medical procedures and study, the research of such as health food, hereditary screening and prevention ahead of time etc., the morbidity possible for futurity actively prevents especially. It 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 smeared and antioxidation foodstuff/medicine etc.

It has been investigated that: human body because of a variety of causes, (such as disease, diet, local environment or living habit) the unease oxygen (O+) of derivation, also known as free radical (harmful free radicals), it is possible to be mixed into water partly with the hydrogen sucked, and excrete. Indirectly reduce the quantity of human free radical, reach acidic physique and be reduced to the alkaline body constitution of health, it is possible to antioxidation, aging resistance, and then also reach to eliminate chronic disease and aesthetic health care effect. Clinical experiment is even had to show, for the patient of some lying on bed for a long time sick beds, because breathing high concentration oxygen for a long time, the injury of lung caused, it is possible to through sucking hydrogen to alleviate the symptom of injury of lung.

But, it is generally of higher temperature via hydrogen and oxygen gas mixture produced after electrolysis unit electrolysis electrolysis water and accompanies electrolyte, it is not appropriate for human body and is directly sucked in. Meanwhile, the problem having electrolyte consumption in electrolytic process produces.

Summary of the invention

Therefore, one of viewpoint of the present invention is in that to provide a kind of gas generator, and it comprises electrolysis unit and a condensate filter. Electrolysis unit is equipped with an electrolysis water. Electrolysis unit in order to electrolysis electrolysis water to produce a hydrogen and oxygen gas mixture. Condensate filter is in order to condense hydrogen and oxygen gas mixture the impurity filtering in hydrogen and oxygen gas mixture. Condensate filter has a blowhole and a venthole, and blowhole is in order to receive hydrogen and oxygen gas mixture, and venthole is in order to discharge the hydrogen and oxygen gas mixture after filtration. Wherein the venthole of condensate filter can be used to input a benefit and is filled with water to electrolysis unit.

Impurity backwashes to electrolysis unit via blowhole optionally through supplementary water.

When electrolysis unit suspends electrolysis electrolysis water to produce hydrogen and oxygen gas mixture, impurity can be backwashed to electrolysis unit via blowhole by supplementary water.

Condensate filter is selectively included multiple condensate film. Each condensate film has a runner. The runner of condensate film is interconnected with the runner of adjacent condensate film, so as to forming the circulatory flow for hydrogen and oxygen gas mixture circulation.

Runner can be formed by a gradual-enlargement type runner and a connection runner. The gradual-enlargement type runner of condensate film can pass through the connection runner of condensate film to be interconnected with the gradual-enlargement type runner of adjacent condensate film.

Gradual-enlargement type runner can be the runner of a cross section flaring. Gradual-enlargement type runner can comprise an opening. Connection runner can have a runner and two corresponding openings. Two corresponding openings of connection runner by runner to be interconnected. The opening of the gradual-enlargement type runner of condensate film can pass through two corresponding openings of the connection runner of condensate film to be interconnected with the opening of the gradual-enlargement type runner of adjacent condensate film.

Circulatory flow is optionally communicated between blowhole and venthole.

Runner is optionally provided with an activated carbon fiber, in order to filter the impurity in hydrogen and oxygen gas mixture.

Runner is optionally separately provided with arbitrary filtering material being made up of pottery, quartz, kieselguhr, meerschaum or combination of the above.

Furthermore, the gas generator of the present invention optionally separately includes a water tank. Water tank has one first hollow bulb and a conduit. Electrolysis unit is arranged within the first hollow bulb of water tank, and conduit is connected to the blowhole of condensate filter, in order to export hydrogen and oxygen gas mixture to condensate filter.

When electrolysis unit suspends this electrolysis water of electrolysis to produce this hydrogen and oxygen gas mixture, the venthole of condensate filter can be used to input this supplementary water, and impurity can also be backwashed to electrolysis unit and the first hollow bulb via blowhole and conduit by supplementary water.

The generation flow rate of the hydrogen and oxygen gas mixture of gas generator is optionally between 0.01L/min. and 12L/min..

Furthermore, the gas generator of the present invention optionally separately comprises one atomization/volatilization gas mixing channel, wherein this atomization/volatilization gas mixing channel couples this venthole of this condensate filter, to receive the hydrogen and oxygen gas mixture after this filtration, wherein this atomization/volatilization gas mixing channel produces an atomization gas and mixes with the hydrogen and oxygen gas mixture after this filtration, to form a health care gas for the suction of this user, wherein this atomization gas is selected from by water vapour, atomization liquid medicine, volatile spirits and combination, the one in the group formed.

Comprehensive, the focusing on of the present invention proposes a kind of gas generator, and it comprises electrolysis unit and condensate filter. In the gas generator of the present invention, hydrogen and oxygen gas mixture produced by electrolysis unit can be undertaken condensing and filter impurity therein by condensate filter, to provide one to be suitable for the hydrogen and oxygen gas mixture that human body sucks. Being designed to supplementary water and backwashing electrolyte to electrolysis unit by the present invention, in order to reduce electrolytical consumption and to avoid electrolyte to block in condensate filter.

Accompanying drawing explanation

Figure 1A and Figure 1B is the schematic diagram of the gas generator illustrating present invention different visual angles in the first specific embodiment;

The schematic diagram of different visual angles when Fig. 2 A and Fig. 2 B is only have tank upper cover and electrolysis unit combination in Figure 1A illustrated embodiment;

The schematic diagram of different visual angles when Fig. 3 A and Fig. 3 B is only have electrolysis unit and the combination of water tank cell body in Figure 1A illustrated embodiment;

Fig. 4 A and Fig. 4 B is the electrolysis unit illustrating gas generator of the present invention explosive view of different visual angles in Figure 1A illustrated embodiment;

Fig. 5 A and Fig. 5 B is that the water tank cell body of the gas generator illustrating the present invention and the electrolysis unit top view in embodiment shown in Fig. 3 A and the line A-A along this top view cut open the profile set;

The schematic diagram of different visual angles when Fig. 6 is only have cell body, dividing plate and combination of electrodes in Figure 1A illustrated embodiment;

Fig. 7 A and Fig. 7 B is that the water tank cell body of the gas generator illustrating the present invention and the electrolysis unit top view in embodiment shown in Fig. 3 A and the line B-B along this top view cut open the profile set;

Fig. 8 is the gas generator illustrating present invention schematic diagram in the second specific embodiment;

Fig. 9 A and Fig. 9 B is the schematic diagram of the gas generator illustrating present invention different visual angles in the tenth specific embodiment;

The schematic diagram of different visual angles when Figure 10 A and Figure 10 B is only have condensate filter and water tank cover assembling in Fig. 9 A illustrated embodiment;

Figure 11 illustrates schematic diagram when not having water tank lid in Figure 10 A illustrated embodiment;

Figure 12 illustrates schematic diagram when not having drainage screen in embodiment illustrated in fig. 11;

Figure 13 illustrates the schematic diagram not having in embodiment illustrated in fig. 12 when filtering square;

Figure 14 A and Figure 14 B is the condensate filter top view in embodiment shown in Figure 10 A of the gas generator illustrating the present invention and the line C-C along this top view cuts open the profile set;

Figure 15 A and Figure 15 B is the schematic diagram of the gas generator illustrating present invention different visual angles in the 14th specific embodiment;

Figure 16 is the schematic diagram illustrating and only having humidification device in Figure 15 A illustrated embodiment;

Figure 17 is the gas generator illustrating present invention schematic diagram in the 5th specific embodiment;

Figure 18 A and Figure 18 B is the schematic diagram of the gas generator illustrating present invention different visual angles in the 15th specific embodiment;

Figure 19 is the gas generator illustrating present invention rearview in embodiment shown in Figure 18 A;

Figure 20 A and Figure 20 B is the top view illustrating and only having condensate filter and water tank lid in Figure 18 A illustrated embodiment and the line D-D along this top view cuts open the profile set.

About advantages 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: electrolysis water W2: supplement water

G: hydrogen and oxygen gas mixture G2: atomization gas

H: hydrogen water

1: gas generator 2: water tank

20: the first hollow 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: fixing post

324: the four hollow bulb 326: the four peristomes

33: electrode column 34: multiple electrodes

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: connection 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 advantages of the present invention, spirit can be easier to and be expressly understood that with feature, follow-up will be described in detail and discussion with embodiment and with reference to appended accompanying drawing. It should be noted that these embodiments are only the representational embodiment of the present invention, the ad hoc approach wherein illustrated, device, condition, material etc. is not limited to the embodiment of 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 of the gas generator illustrating present invention different visual angles in the first specific embodiment, the schematic diagram of different visual angles when Fig. 2 A and Fig. 2 B is only have tank upper cover and electrolysis unit combination in Figure 1A illustrated embodiment, as shown in the figure, in first embodiment, gas generator 1 of the present invention includes water tank 2 and electrolysis unit 3. Water tank 2 is equipped with an electrolysis water W, and electrolysis unit 3 is arranged in water tank 2, in order to electrolysis this electrolysis water 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 electrolysis water W, electrolysis water W riddles the first hollow bulb of water tank 2 and is in full-water level, when after electrolysis unit 3 electrolysis electrolysis water W, electrolysis water W fill the first hollow bulb of water tank 2 water level higher than the 90% of full-water level. Hereinafter the design of each element to the present invention is first illustrated respectively.

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 adapted for holding an electrolysis water W. Electrolysis water W Main Ingredients and Appearance is pure water, optionally can add a small amount of electrolyte, such 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, in order to export produced by electrolysis unit 3 hydrogen and oxygen gas mixture G and to supplement input this electrolysis water W in water tank 2.

Further, referring to Fig. 3 A and Fig. 3 B, Fig. 3 A and Fig. 3 B is the water tank of the gas generator illustrating present invention explosive view of different visual angles in specific embodiment shown in Figure 1A. 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 extends toward its normal vector direction from the inner surface of the first base 240 to form outward, and the first wall portion 242 encloses to be provided 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 two surfaces relative to electrolysis unit 3 direction, the first wall portion 242 of joining water box cell body 24, and the water inlet 249b of water tank cell body 24 is two surfaces relative to electrolysis unit 3 direction, the first wall portion 242 of joining water box cell body 24. Wherein, the outlet 249a of water tank the cell body 24 and water inlet 249b of water tank cell body 24 is connected by the first hollow bulb 20. The outlet 249a and a water inlet 249b of water tank cell body 24 may be used to be interconnected for the first hollow bulb 20 of a pumping plant with 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 extends toward its normal vector direction from the inner surface of the second base 260 to form outward, and the second wall portion 262 encloses to be provided with one second hollow bulb 264, and the second hollow bulb 264 is have one second peristome 266 relative to the other end of the second base 260. First lateral margin 248 of water tank cell body 24 can be covered in the second hollow bulb 264 by water tank lid 26 by the second peristome 266. Conduit 22 may be disposed at second base 260, two surfaces relative to water tank cell body 24 direction of also joining water box lid 26 on the second base 260 of water tank lid 26, but it is not limited, when practical application, conduit 22 can also by a guide hole or other to have the element of input/output function 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 lids 26 is relative to two surfaces in water tank cell body 24 direction, run through and be arranged at electrolysis unit 3 in order to the electrode column of electrolysis device 3, or run through with for detecting device (such as flow rate detector, water-level gauge, relief valve) and be arranged on.

Further, in the present embodiment, water tank 2 separately includes a sealing gasket 28, and it is disposed between water tank cell body 24 and water tank lid 26, in order to make water box slot body 24 and water tank lid 26 combine closely. 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 that multiple cap bore 261 and the second peristome 266 are enclosed and are located therein. The corresponding surface of water tank cell body 24 and sealing gasket 28 more can be respectively provided with one first embedded structure 246 and the 3rd corresponding embedded structure 282 and its both be able to mutually chimeric. First embedded structure 246 is to enclose the first peristome 244 to be located therein. 3rd embedded structure 282 is to enclose the 3rd peristome 280 to be located therein.

Then, referring to Fig. 4 A and Fig. 4 B, Fig. 4 A and Fig. 4 B is the electrolysis unit illustrating gas generator of the present invention explosive view of different visual angles in Figure 1A illustrated embodiment. Electrolysis unit 3 comprises a cell body 32, multiple electrode 34, backing plate 36, upper cover body 37 and lower cover 38. Plurality of electrode 34 is respectively separated and is arranged within cell body 32 and is formed 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 backing plate 36 other end relative to cell body 32. Lower cover 38 is covered on the lower surface other end relative to upper cover body 37 of cell body 32.

Further, refer to water tank cell body and the electrolysis unit top view in the embodiment of embodiment shown in Fig. 3 A that Fig. 5 A and five B, Fig. 5 A and Fig. 5 B is the gas generator illustrating the present invention and the line A-A along this top view cuts open the profile set. Electrolysis unit separately has a dividing plate 30. Dividing plate 30 is to extend outward toward its normal vector direction relative to the side surface of water tank 2 from cell body to form, in order to the first hollow bulb 20 of water tank 2 to be separated into top 200 and a bottom 202. Dividing plate 30 comprises an intercommunicating pore 300. Intercommunicating pore 300 connects the dividing plate 30 two surfaces 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 to be interconnected by intercommunicating pore. But the design of intercommunicating pore is not limited with this enforcement depicted, when practical application, the quantity of intercommunicating pore or external form all visually use actual demand to select design voluntarily.

Then, the schematic diagram of different visual angles when Fig. 6, Fig. 6 are only have cell body, dividing plate and combination of electrodes in Figure 1A illustrated embodiment is referred to. Cell body 32 is roughly divided into one the 4th base 320 and a fourth wall 322. Fourth wall 322 is to extend outward toward its normal vector direction from the inner surface of the 4th base 320 to form, and fourth wall 322 is to enclose to be provided 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 to accommodate this electrolysis water W. It addition, for the design expressing cell body of the present invention, be purposely economize multiple electrodes slightly therein in Fig. 6, but, when practical application, design is selected in the upper actual demand of visual use 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 are the water tank cell body of the gas generator illustrating the present invention and the electrolysis unit top view in embodiment shown in Fig. 3 A and the line B-B along this top view cut open the profile set. 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 connect the 4th base 320 two surfaces 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 grooves 3204 are to extend inside along normal vector direction relative to the surface of the 4th peristome 326 from the 4th base 320 of cell body 32 to form. Each groove 3204 is to be spaced between lower perforation 3202 and adjacent lower perforation 3202. Multiple grooves 3204 may be used to place electrode 34. Meanwhile, the fourth wall 322 of cell body 32 separately has multiple fixing post 3220. Multiple fixing posts 3220 are to extend outward toward its normal vector direction relative to the surface of multiple lower perforation 3202 from fourth wall 322 to form. Fixing post 3220 may be used to fixed placement in the electrode 34 of groove 3204 with adjacent fixing post 3220. When multiple electrodes 34 are respectively separated and are arranged in the groove 3204 of cell body 32 and are fixed between fixing post 3220 and adjacent fixing post 3220, multiple electrode runner S1 within cell body 32, can be formed. Each of which electrode runner S1 can be connected 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 are the connection backing plate 36 two surfaces relative to cell body 32 direction. Further, each electrode runner S1 also can be connected by the top 200 of corresponding upper perforation 360 with the first hollow bulb 20 independently of one another.

Multiple electrodes 34 include cathode sheets 340, anode strip 342 and multiple bipolar electrode sheet 344. Multiple bipolar electrode sheets 344 are to be 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 may connect to the negative pole of power supply, and anode strip 342 may connect to the positive pole of power supply, and the voltage difference of the one group of electrolysis electrode being 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 constituted is about between 1.5V��3V. In another embodiment, the voltage difference of one group of electrolysis electrode that bipolar electrode sheet 344 is constituted with adjacent bipolar electrode sheet 344 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 constituted 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 is to extend inside along normal vector direction relative to the surface of backing plate 36 from upper cover body 37 to form. The multiple upper perforation 360 and the first hollow bulb 20 that are positioned at backing plate 36 are to be interconnected by this 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 is to extend inside along normal vector direction relative to the surface of the 4th base 320 of cell body 32 from lower cover 38 to form. The multiple lower perforation 3202 of the 4th base 320 being positioned at cell body 32 is be interconnected by this at least one second runner 380 with this first hollow bulb 20.

Further, it is please the gas generator illustrating present invention schematic diagram in the second specific embodiment referring initially to Fig. 8, Fig. 8. In the second specific embodiment, the gas generator 1 of the present invention separately comprises a pumping plant 5 (only illustrating in Fig. 8) with dotted line. Pumping plant 5 may be used to the electrolysis water W that forced circulation is placed in the first hollow bulb 20. Pumping plant 5 comprises oral siphon 50 and an outlet pipe 52. The outlet pipe 52 of pumping plant 5 is connected with each other 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 connected with each other in order to the outlet 249a of feed pump device 5 with this water tank 2.

Further, in the 3rd specific embodiment, the 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 may connect 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, to form a health care gas for the suction of this user. When practical application, atomization gas G2 can be selected from by water vapour, atomization liquid medicine, volatile spirits and combination, the one in the group formed.

Above, to each element each design illustrate after, below the compound mode of each element to a kind of gas generator and its application are described.

In the electrolysis unit 3 being completed, multiple electrodes 34 are respectively separated and are arranged at cell body 32, backing plate 36 is arranged at the upper surface of each electrode 34, upper cover body 37 is covered on the backing plate 36 other end relative to cell body 32, and lower cover 38 is covered on the lower surface other end relative to upper cover body 37 of cell body 32.

In the water tank 2 being completed 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 detecting device (such as flow rate detector 82) is by through multiple cap bore 261 of water tank lid 26 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 being completed, electrolysis unit 3 and pumping plant 5, water tank 2 and pumping plant 5 are that the connection of the outlet 249a of the connection of water inlet 249a of the outlet pipe 52 by pumping plant 5 and water tank 5 and the oral siphon 50 of pumping plant 5 and water tank 5 is to be interconnected. Further, in the 3rd embodiment, atomization/volatilization gas mixing channel 4 is to connect electrolysis unit 3.

When practical application, water tank 2 is equipped with an electrolysis water W, and electrolysis unit 3 is arranged in water tank 2, in order to electrolysis this electrolysis water 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. Input exports via the conduit 22 of water tank 2 further to the hydrogen and oxygen gas mixture G of the first hollow bulb 20, and be available for users to suck, but it is not limited, when practical application, input can mix with the atomization gas G2 produced via atomization/volatilization gas mixing channel 4 further to the hydrogen and oxygen gas mixture G of the first hollow bulb 20, to form health care gas for user suction.

It addition, when electrolysis unit 3 suspends electrolysis electrolysis water W to produce hydrogen and oxygen gas mixture G, conduit 22 can be used to supplement input electrolysis water W, so that electrolysis water W is full of the first hollow bulb 20 and/or electrolysis unit 3. The electrolysis water W supplementing input the first hollow bulb 20 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, electrolysis water 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 electrolysis water is full of the first hollow bulb of water tank in one embodiment. In an embodiment, when electrolysis unit 3 starts electrolysis electrolysis water W, electrolysis water W is filled with being in full-water level in the first hollow bulb of water tank 2, when, after electrolysis unit 3 electrolysis electrolysis water W, electrolysis water W fills the water level of the first hollow bulb of water tank 2 higher than the 90% of full-water level. In an embodiment, gas generator of the present invention can pass through water-level gauge and detect the water level in the first hollow bulb and/or electrolysis unit being placed in water tank, to control whether supplementing of electrolysis water, make the water level of the first hollow bulb of electrolysis water filling water tank higher than the 90% of full-water level. Therefore the design of gas generator of the present invention is avoided that air cavity is present in water tank, the temperature of electrolysis unit more can be made to reduce, thus reducing the risk of high temperature air blasting and improving its safety.

It 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 electrolysis water W in the first hollow bulb 20 in order to forced circulation. Being positioned at the top 200 of the first hollow bulb 20 with the electrolysis water of bottom 202 is be circulated via intercommunicating pore 300. Wherein, when, after electrolysis unit electrolysis electrolysis water W, electrolysis water W fills the water level of the first hollow bulb 20 of water tank 2 higher than the 90% of full-water level. Further, the design of gas generator of the present invention can be placed in the electrolysis water in the first hollow bulb by forced circulation, makes 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.

It 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 can selectively cut off the electrical connection of electrolysis unit 3 and power supply (not being illustrated in figure).

In sum, in the present invention, electrolysis unit is arranged at the design of water tank and can save space, the hydrogen and oxygen gas mixture that electrolysis unit produces simultaneously is by riddling the electrolysis water of the first hollow bulb of water tank, air cavity can be avoided to be present in water tank, the temperature that can also make electrolysis unit reduces, thus preventing the generation of air blasting. Furthermore, the gas outlet of electrolysis unit and water inlet design in the present invention so that the electrolysis water in water tank can be supplemented to electrolysis unit, and hydrogen and oxygen gas mixture produced by electrolysis unit can be expelled to water tank, reaches air water circulation. Further, in the present invention, the structural design that pumping plant, water tank and electrolysis unit are interconnected, the electrolysis water being placed in the first hollow bulb can be made to 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 be the gas generator of a kind of effect with the electrolysis water after regulation and control electrolysis coolant-temperature gage and cooling generation 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 an electrolysis water W. Electrolysis unit 3 in order to electrolysis electrolysis water W to produce a hydrogen and oxygen gas mixture G. Chiller 7 is connected to electrolysis unit 3, in order to cool down the electrolysis water W after producing hydrogen and oxygen gas mixture G. Pumping plant 5 is connected between chiller 7 and electrolysis unit 3, in order to forced circulation electrolysis water W.

Referring to Figure 17, Figure 17 is the gas generator illustrating present invention schematic diagram in the 5th specific embodiment. In the 5th specific embodiment, the 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 electrolysis water W. Electrolysis unit 3 is disposed within the first hollow bulb 20 of water tank 2, and the first hollow bulb 20 is be interconnected with electrolysis unit 3. But being not limited, in another embodiment (as shown in Fig. 3 B, Fig. 5 B and Fig. 8), the gas generator 1 of the present invention separately comprises a dividing plate 30. Dividing plate 30 comprises an intercommunicating pore 300. Dividing plate 30 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. Intercommunicating pore is passed through to be interconnected in top 200 and bottom 202. 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 the electrolysis water in top 200 and bottom 202 and can pass through water hydrargyrum device 5 to carry out forced circulation. In different embodiments, 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, the 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, to form health care gas for the suction of this user.

Hereinafter the design of each element to the present invention is first illustrated respectively.

Firstly, since the structural design of water tank 2, electrolysis unit 3, pumping plant 5 and atomization/volatilization gas mixing channel 4 is in explanation made above, therefore do not repeat again at this.

Refer to Figure 15 A, Figure 15 B and Figure 17. In the 4th embodiment, the 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 is distributed across within the casing 700 of radiator 70. Radiating tube 702 be shaped as a coil (not being illustrated in figure), 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. Additionally, when practical application, radiating tube 702 can made by one of silver, aluminum, ferrum, copper, silver alloy, aluminium alloy, ferroalloy, the above material of copper alloy. Further, radiator 70 comprises entrance 704 and an outlet 706. The entrance 704 of radiator 70 is the casing 700 connecting this radiator 70 two surfaces relative to radiating tube 702 direction, and the outlet 706 of radiator 70 is the casing 700 connecting this radiator 70 two surfaces relative to radiating tube 702 direction. Wherein, the entrance 704 of radiator 70 and outlet 706 are to be interconnected by radiating tube 702.

Further, in the 4th embodiment, the gas generator 1 of the present invention separately comprises a microcomputer controller (not being illustrated in figure). Microcomputer controller is the temperature sensing electrolysis water W, and according to the temperature of the electrolysis water W sensed to control the flow velocity that pumping plant 5 extracts and inputs. It addition, microcomputer controller comprises a temperature-sensitive sticker (not being illustrated in figure). Temperature-sensitive sticker is the temperature sensing the electrolysis water W being placed in electrolysis unit 3. Additionally, microcomputer controller separately comprises a flow rate detector 82. Flow rate detector 82 is 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 can selectively 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 illustrated, compound mode and its application of each element will be described below.

In the water tank 2 being completed 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. Further, since the compound mode of the water tank 2 being completed and electrolysis unit 3 is in explanation made above, therefore do not repeat again at this.

In the water tank 2 being completed, 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 it is not limited, when practical application, radiator 70 may be directly connected to electrolysis unit 3, pumping plant 5 may be directly connected between radiator 7 and water tank 2, imply that the gas generator of the present invention does not need water tank 2, or do not need electrolysis unit 3 is arranged at the gas generator that can also complete the present invention in water tank 2.

Then, the above-mentioned water tank 2 being completed, electrolysis unit 3, annexation between pumping plant 5 and chiller 7 are further described. Refer to Figure 15 A and Figure 15 B. It is provided with the entrance 704 that the outlet 249a of the water tank 2 of electrolysis unit 3 is radiator 70 with chiller 7 to be connected with each other, the outlet 706 of the radiator 70 of chiller 7 is that the oral siphon 50 with pumping plant 5 is connected with each other, and the water inlet 249b that the outlet pipe 52 of pumping plant 5 is with water tank 2 is connected with each other. But it is not limited with above-mentioned annexation, when practical application, the outlet 249a of the water tank 2 being provided with electrolysis unit 3 can be connected with each other with the oral siphon 50 of pumping plant 5, the outlet pipe 52 of pumping plant 5 can be connected with each other with the entrance 704 of the radiator 70 of chiller 7, and the outlet 706 of the radiator 70 of chiller 7 can be connected with each other with the water inlet 249b of water tank 2.

When practical application, water tank 2 is equipped with an electrolysis water W, and electrolysis unit 3 is arranged in water tank 2, in order to electrolysis electrolysis water 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. Input exports via the conduit 22 of water tank 2 further to the hydrogen and oxygen gas mixture G of the first hollow bulb 20, and be available for users to suck, but it is not limited, when practical application, the hydrogen and oxygen gas mixture G exported by the first hollow bulb 20 can mix with the atomization gas G2 produced via atomization/volatilization gas mixing channel 4 further, to form health care gas for user suction.

It addition, when electrolysis unit 3 suspends electrolysis electrolysis water W to produce hydrogen and oxygen gas mixture G, conduit 22 can be used to supplement input electrolysis water W, so that electrolysis water W is full of the first hollow bulb 20 and/or electrolysis unit 3. The electrolysis water W supplementing input the first hollow bulb 20 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, electrolysis water W required during to provide electrolysis unit 3 electrolysis.

It addition, water tank 2, electrolysis unit 3, pumping plant 5 and chiller 7 are to be interconnected. When application, produce the electrolysis water W after hydrogen and oxygen gas mixture G and can pass through pumping plant 5 from the outlet 249a pressure output of water tank 2 to the entrance 704 of the radiator 70 of chiller 7, and cool down in the radiating tube 702 of radiator 70. Electrolysis water W after cooling can pass through pumping plant 5 and export the oral siphon 50 to pumping plant 5 via outlet 706 pressure of radiator 70, further, this electrolysis water W can force to input the water inlet 249b to water tank 2 via the outlet pipe 52 of pumping plant 5 by pumping plant 5. Therefore, the gas generator of the present invention can pass through the electrolysis water after chiller cooling produces hydrogen and oxygen gas mixture, and put by force this electrolysis water of circulation by pumping plant, to reach effect of heat radiation. Wherein, the temperature of this electrolysis water being placed in this electrolysis unit is a conventional electrolysis temperature, and when practical application, the temperature of the electrolysis water W being placed 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 electrolysis water W, and according to the temperature of the electrolysis water W sensed to control the flow velocity that pumping plant 5 extracts and inputs. When practical application, when the temperature of the electrolysis water W sensed via temperature-sensitive sticker 80 is higher than a preset temperature, the too high information of this temperature can be communicated back to microcomputer controller 8, then microcomputer controller 8 can control pumping plant 5 further to accelerate the flow velocity of electrolysis water W circulation, makes the temperature of electrolysis water reduce to return in preset temperature. On the contrary, when the temperature of the electrolysis water W sensed via temperature-sensitive sticker 80 is lower than a preset temperature, the too low information of this temperature can be communicated back to microcomputer controller 8, then microcomputer controller 8 can control pumping plant 5 further to slow down the flow velocity of electrolysis water W circulation, makes the temperature of electrolysis water raise to return in preset temperature. Wherein preset temperature is the temperature being provided that 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, the focusing on of the present invention proposes a kind of gas generator, and it comprises electrolysis unit, chiller and pumping plant. The gas generator of the present invention can pass through the electrolysis water after chiller cooling produces hydrogen and oxygen gas mixture, and puts by force cyclic electrolysis water by pumping plant, to reach effect of heat radiation. Meanwhile, the present invention can make electrolysis coolant-temperature gage be positioned at the temperature range of offer the best electrolytic efficiency, produces the hydrogen and oxygen gas mixture problem to solve power consumption in order to electrolysis electrolysis water effectively.

It addition, in an embodiment, water tank 2, electrolysis unit 3, pumping plant 5 and radiator 70 are to be interconnected. First hollow bulb 20 is divided into top 200 and a bottom 202 by dividing plate 30. When application, producing the electrolysis water W after hydrogen and oxygen gas mixture G can force output to the entrance 704 of radiator 70 by pumping plant 5 from the outlet 249a on the top 200 being positioned at water tank 2, and cools down in radiator 70. Electrolysis water W after cooling can pass through pumping plant 5 and export the oral siphon 50 to pumping plant 5 via outlet 706 pressure of radiator 70, further, this electrolysis water W can force to input to the water inlet 249b being positioned at water tank 2 bottom 202 via the outlet pipe 52 of pumping plant 5 by pumping plant 5. Therefore, the gas generator of the present invention can pass through the electrolysis water after radiator cooling produces hydrogen and oxygen gas mixture, and put by force the electrolysis water in the top circulating the first hollow bulb being placed in water tank and bottom by pumping plant, 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. Accommodating electrolysis water W (not being illustrated in figure) of electrolysis unit 3. Electrolysis unit 3 in order to electrolysis electrolysis water W to produce a hydrogen and oxygen gas mixture G. Condensate filter 6 connects electrolysis unit 3, in order to condense hydrogen and oxygen gas mixture G the impurity filtering in hydrogen and oxygen gas mixture G. Condensate filter 6 can be used to input supplementary water W2 (not being illustrated in figure) to electrolysis unit 3. In an embodiment, when electrolysis unit 3 suspends electrolysis electrolysis water W to produce hydrogen and oxygen gas mixture G, condensate filter 6 can be used to input supplementary water W2, and impurity can pass through to supplement water W2 and backwash to electrolysis unit 3 via condensate filter 6.

Further, in the 8th specific embodiment, the 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 electrolysis water W. Electrolysis unit 3 is disposed within the first hollow bulb 20 of water tank 2.

Further, in the 9th specific embodiment, the 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 receive the hydrogen and oxygen gas mixture G after filtration. Atomization/volatilization gas mixing channel 4 can produce atomization gas G2 and filter after hydrogen and oxygen gas mixture G mix, with is formed health care gas confession this user suction.

Refer to the schematic diagram that Fig. 9 A and Fig. 9 B, Fig. 9 A and Fig. 9 B is the gas generator illustrating present invention different visual angles in the tenth specific embodiment. In the tenth specific embodiment, the gas generator 1 of the present invention can separately comprise a pumping plant 5 and chiller 7.

Firstly, since the structural design of water tank 2, electrolysis unit 3 and atomization/volatilization gas mixing channel 4 is in explanation made 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. The condensate filter 6 of the present invention has blowhole 60 and a venthole 62. Blowhole 60 may connect 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 filtration. It addition, the 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 condensate film 64 is interconnected with the runner 640a of adjacent condensate film 64, so as to forming the circulatory flow 640 for hydrogen and oxygen gas mixture G circulation, in order to condense hydrogen and oxygen gas mixture G. Blowhole 60 and venthole 62 can pass through circulatory flow 640 and be interconnected. In an embodiment, the runner 640a of condensate film 64 connects runner 644 by a gradual-enlargement type runner 642 with one and is formed. 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 one end of relatively wide one end and opposite, narrow. Relatively wide one end of gradual-enlargement type runner 642 and one end of opposite, narrow all have an opening. Connection runner 644 has a runner and two corresponding openings. Two corresponding openings of connection runner 644 can be interconnected by runner. When gradual-enlargement type runner 642 with connect runner 644 be connected with each other time, gradual-enlargement type runner 642 is interconnected with the connection of the opening connecting runner 644 by the relatively wide opening of one end of gradual-enlargement type runner 642 with connecting runner 644. 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 (namely connecting runner 644), but horizontal run is not limited with the runner of cross section flaring, when practical application, horizontal run can also be the runner that cross section is equal. Further, when the runner 640a of condensate film 64 is connected with each other with the runner 640a of adjacent condensate film 64, the runner 640a of the condensate film 64 and runner 640a of adjacent condensate film 64 is interconnected by the connection of the opening of one end of the opposite, narrow of the gradual-enlargement type runner 642 of condensate film 64 with the opening of the connection runner 644 of adjacent condensate film 64. Therefore, the structural design of the runner 640a of condensate film 64, it makes the runner 640a of condensate film 64 be interconnected with the runner 640a of adjacent condensate film 64, so as to forming the circulatory flow 640 for hydrogen and oxygen gas mixture circulation. Imply that in the present embodiment, the connected mode of condensate film and adjacent condensate film, hydrogen and oxygen gas mixture can be ordered about and pass through longer condensation and filtration path, and then reach condensation more preferably and filter effect. Further, in an embodiment, an activated carbon fiber in runner 640a, can be provided with, in order to filter the impurity in hydrogen and oxygen gas mixture G. Runner 640a can separately be provided with arbitrary filtering material being made up of pottery, quartz, kieselguhr, meerschaum or combination of the above, and filtering material can further filter the impurity in hydrogen and oxygen gas mixture G. Wherein impurity is the electrolyte in electrolysis water W, and it is sodium hydroxide. But being not limited, when practical application, impurity can be calcium carbonate, sodium chloride etc. Additionally, in an embodiment, the 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 may connect 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 to be placed in water tank 2 in order to be connected with condensate filter 6 further.

In the water tank 2 being completed, electrolysis unit 3 and condensate filter 6, the water tank 2 and the condensate filter 6 that are provided with electrolysis unit 3 are that the connection between the conduit 22 by water tank 2 and the blowhole 60 of condensate filter 6 is to be interconnected. Further, atomization/volatilization gas mixing channel 4 may connect to the venthole 62 of condensate filter 6.

When practical application, water tank 2 is equipped with an electrolysis water W, and electrolysis unit 3 is arranged in water tank 2, in order to electrolysis electrolysis water 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. Input exports via the conduit 22 of water tank 2 further to the hydrogen and oxygen gas mixture G of the first hollow bulb 20. 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 to carry out condensing and filtering. First the hydrogen and oxygen gas mixture G of the blowhole 60 of entrance condensate filter 6 can first pass through drainage screen 600 and filtration square 602 preliminarily filters. Then, carry out the hydrogen and oxygen gas mixture G after preliminarily filtering to condense further into circulatory flow 640, meanwhile, hydrogen and oxygen gas mixture G can pass through to be arranged at the activated carbon fiber in runner 640a and filtering material is filtered and can be adsorbed in circulatory flow by impurity in 640. Then, hydrogen and oxygen gas mixture G after filtration can pass through the hydrogen and oxygen gas mixture G after venthole 62 output filtering of condensate filter 6, and be available for users to suck, but it is not limited, when practical application, hydrogen and oxygen gas mixture G after the filtration exported by condensate filter 6 can mix with the atomization gas G2 produced via atomization/volatilization gas mixing channel 4 further, to form health care gas for user suction.

It addition, in an embodiment, when electrolysis unit 3 suspends electrolysis electrolysis water W to produce hydrogen and oxygen gas mixture G, the venthole 62 of condensate filter 6 can be used to input to supplement water W2. The supplementary water W2 supplemented by the venthole 62 of condensate filter 6 can input to the first hollow bulb 20 of water tank 2 via the conduit 22 being connected with venthole 62. The electrolysis water W supplementing input the first hollow bulb 20 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, electrolysis water W required during to provide electrolysis unit 3 electrolysis. And be adsorbed in the impurity in the circulatory flow 640 of condensate filter 6 and can also be backwashed to the water tank 2 being provided with electrolysis unit 3 via blowhole 60 and conduit 22 by above-mentioned supplementary water W2.

It 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, the focusing on of the present invention proposes a kind of gas generator, and it comprises electrolysis unit and condensate filter. In the gas generator of the present invention, hydrogen and oxygen gas mixture produced by electrolysis unit can be undertaken condensing and filter impurity therein by condensate filter, to provide one to be suitable for the hydrogen and oxygen gas mixture that human body sucks. Meanwhile, it is designed to while supplementary water to backwash electrolyte to electrolysis unit by 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 11st 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 electrolysis water W, in order to electrolysis electrolysis water 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 12nd specific embodiment, the 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, in order to condense hydrogen and oxygen gas mixture G produced by electrolysis unit 3 impurity filtering in hydrogen and oxygen gas mixture G. The humidification device 9 hydrogen and oxygen gas mixture in order to receive and after humidifying filtration.

Further, in the 13rd specific embodiment, the gas generator 1 of the present invention separately comprises one atomization/volatilization gas mixing channel 4. Atomization/volatilization gas mixing channel 4 may connect to the humidification device being connected with condensate filter, in order to receive the hydrogen and oxygen gas mixture G filtered and after 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, to form health care gas for user suction. But being not limited, in another embodiment, atomization/volatilization gas mixing channel 4 may connect 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, to form health care gas for user suction. But being not limited, in an embodiment, the 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, to form health care gas for user suction. But being not limited, in another embodiment, hand-hold atomization device can connect the humidification device being connected with condensate filter, in order to receive the hydrogen and oxygen gas mixture filtered and after humidifying. Hand-hold atomization device produces atomization gas and mixes with the hydrogen and oxygen gas mixture after filtration and humidifying, to form health care gas for user suction. 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 being made up of water vapour, atomization liquid medicine, volatile spirits and combination thereof.

Refer to the schematic diagram that figure 15, Figure 15 A and Figure 15 B is the gas generator illustrating present invention different visual angles in the 14th specific embodiment. Further, in the 14th specific embodiment, the 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 may be used to output health care gas for user suction, and health care gas is the mixing of the hydrogen and oxygen gas mixture G after humidifying and atomization gas G2.

Firstly, since the structural design of condensate filter 6 and atomization/volatilization gas mixing channel 4 is in explanation made above, therefore do not repeat again at this.

The 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), one the 3rd conduit 96 and one the 4th conduit 98. Hollow body 90 may be used to accommodating one and supplements water W2. Second conduit 92 is arranged on hollow body 90 and may be used to be connected (not being illustrated in figure) with electrolysis unit 3. At least one outlet tube 94 is arranged among hollow body 90 and is connected with the second conduit 92. Second conduit 92 is to be connected to form a T-type structure with two outlet tubes 94, but is not limited, and 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 nanometers to 10 nanometers that perforation can have nano level aperture, in order to refine to form diffluent bubble disintegration to gas, but is not limited, when practical application, the visual user demand of pore size of perforation is adjusted. The end of two outlet tubes 94 connecting the second conduit 92 is all respectively arranged with a rubber stopper, in order to make the hydrogen and oxygen gas mixture G received by the second conduit 92 be expelled to hollow body 90 by multiple nanometers of perforation (not being illustrated in figure) of two outlet tubes 94, but it is not limited, when practical application, the end connecting two outlet tubes 94 of the second conduit 92 also can be the design closed. In an embodiment, rocking equipment 95 may be disposed among hollow body 90 and is positioned at the lower section of at least one outlet tube 94, in order to shake supplementary water. Rocking equipment 95 can comprise a sonicator, is used for the supplementary water in hollow body 90 is shaken. 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, any it be arranged on hollow body and water can be shaken or stir effectively to disperse hydrogen and oxygen gas mixture to become the device of micro-bubble, belonging to the rocking equipment that the present invention is defined. Such as, rocking equipment 95 also can comprise centrifugeblade and connect the driving motor of centrifugeblade, drives motor that centrifugeblade can be driven to rotate and produces 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 driving motor, makes the generation of hydrogen water more efficiently. 3rd conduit 96 may be disposed on hollow body 90, in order to export hydrogen water H or to supplement water W2 in order to supplementary input. When practical application, the 3rd conduit can connect a guide hole, by the 3rd conduit by guide hole to pour out hydrogen water H or to pour supplementary water W2 into. 4th conduit 98 may be disposed on hollow body 90, in order to export the hydrogen and oxygen gas mixture G after humidifying.

Further, in another example, the 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 electrolysis water W. Electrolysis unit 3 is disposed within the first hollow bulb 20 of water tank 2. Additionally, the humidification device 9 of the present invention can separately comprise one second water hydrargyrum device (not being illustrated in figure). Second water hydrargyrum device may be disposed on water tank lid 26 and be communicated in the first hollow bulb 20, in order to extract the gas within water tank 2 so that its inside produces a negative pressure.

In an electrolysis unit 3 being completed, multiple electrodes 34 are respectively separated and are arranged at cell body 32, backing plate 36 is arranged at the upper surface of each electrode 34, upper cover body 37 is covered on the backing plate 36 other end relative to cell body 32, and lower cover 38 is covered on the lower surface other end relative to upper cover body 37 of cell body 32.

It is locked on water tank lid 26 separately by two electrode columns 33 in the water tank 2 being completed and electrolysis unit 3, the anode strip 342 of the electrolysis unit 3 after having assembled and cathode sheets 340. And detecting device (such as flow rate detector 82) is by through multiple cap bore 261 of water tank lid 26 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 being completed, 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 that the connection between the conduit 22 by water tank 2 and the blowhole 60 of condensate filter 6 is to be interconnected. Then, and the condensate filter 6 that is interconnected of water tank and humidification device 9 be that the connection between the venthole 60 by condensate filter 6 and the second conduit 92 of humidification device 9 is to be interconnected. Further, in the 13rd specific embodiment, atomization/volatilization gas mixing channel 4 may connect to the 4th conduit 98 of humidification device 9.

When practical application, water tank 2 is equipped with an electrolysis water W, and electrolysis unit 3 is arranged in water tank 2, in order to electrolysis electrolysis water 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. Input exports via the conduit 22 of water tank 2 further to the hydrogen and oxygen gas mixture G of the first hollow bulb 20. 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 to carry out condensing and filtering. First the hydrogen and oxygen gas mixture G of the blowhole 60 of entrance condensate filter 6 can first pass through drainage screen 600 and filtration square 602 preliminarily filters. Then, carry out the hydrogen and oxygen gas mixture G after preliminarily filtering to condense further into circulatory flow 640, meanwhile, hydrogen and oxygen gas mixture G can pass through to be arranged at the activated carbon fiber in runner 640a and filtering material is filtered and can be adsorbed in circulatory flow by impurity in 640. Then, the hydrogen and oxygen gas mixture G after filtration can by the hydrogen and oxygen gas mixture G after venthole 62 output filtering of condensate filter 6.

Furthermore, the hydrogen and oxygen gas mixture G after filtration can be inputted to humidification device 9 by the second conduit 92 being connected with venthole 62. Hydrogen and oxygen gas mixture G after the filtration received by the second conduit 92 can pass through multiple nanometers of perforation of two outlet tubes 94 to be expelled in hollow body 90. When practical application, due to the multiple nanometers of perforation that the surface of outlet tube 94 has, it can be used for the hydrogen and oxygen gas mixture of input humidification device is refined, to form diffluent bubble disintegration. Meanwhile, the supplementary water being placed in humidification device 9 is shaken by rocking equipment 95, in order to allow gas in the supplementary water after being easily dissolved in concussion. Wherein above-mentioned can be passed through the supplementary water after rocking equipment 95 shakes by nanometer hydrogen and oxygen gas mixture G that discharges of perforation and carry out humidifying to produce the hydrogen and oxygen gas mixture after humidifying, and be available for users to suck, but it is not limited, when practical application, hydrogen and oxygen gas mixture G after the humidifying exported by humidification device 9 can mix with the atomization gas G2 produced via atomization/volatilization gas mixing channel 4 further, to form health care gas for user suction. By surface, there is nanometer the hydrogen and oxygen gas mixture G that the outlet tube of perforation discharges also can be combined with the supplementary water after shaking via rocking equipment 95 to produce a hydrogen water H it addition, above-mentioned. More particularly, surface having nanometer hydrogen and oxygen gas mixture G that the outlet tube of perforation is discharged is diffluent bubble disintegration, and the supplementary water after shaking via rocking equipment 95 is for easily to make gas be dissolved in supplementary water therein. Therefore can produce to dissolve the hydrogen water H of higher concentration hydrogen-oxygen through the hydrogen or oxygen gas generator of the present invention.

In addition, in another embodiment, humidification device 9 can be directly entered via hydrogen and oxygen gas mixture produced by electrolysis unit 3 electrolysis electrolysis water W and carry out humidifying. Imply that the hydrogen and oxygen gas mixture 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. Input exports via the conduit 22 of water tank 2 further to the hydrogen and oxygen gas mixture of the first hollow bulb 20. The hydrogen and oxygen gas mixture exported by the conduit 22 of water tank 2 can input to humidification device 9 via the second conduit 92 by being connected with conduit 22 to produce the hydrogen and oxygen gas mixture after humidifying, and is available for users to suck. But being not limited, when practical application, humidification device 9 the hydrogen and oxygen mixture physical ability after the humidifying exported mixes with the atomization gas produced via atomization/volatilization gas mixing channel 4 further, to form health care gas for user suction. By surface, there is nanometer the hydrogen and oxygen gas mixture G that the outlet tube of perforation discharges also can be combined to produce a hydrogen water with the supplementary water after shaking via rocking equipment 95 it addition, above-mentioned.

It addition, when electrolysis unit 3 suspends electrolysis electrolysis water to produce hydrogen and oxygen gas mixture, the gas that the second water hydrargyrum device may be used to extract within water tank 2 is so that its inside produces negative pressure. The supplementary water W2 supplementing input via the 3rd conduit 96 can be inputted back in the water tank 2 being provided with electrolysis unit 3 by humidification device 9 by above-mentioned negative pressure. More particularly, supplement water to be inputted to condensate filter 6 by humidification device 9 by the connection between the second conduit 92 and the venthole 62 of condensate filter 6 of humidification device 9. Further, it is adsorbed in the impurity in the circulatory flow 640 of condensate filter 6 to be backwashed to the water tank 2 being provided with electrolysis unit 3 via blowhole 60 and conduit 22 by above-mentioned supplementary water, in order to recover the filter capacity of circulatory flow, the obstruction preventing circulatory flow and corrosion and to lower electrolytical consumption. In practice, the present invention utilizes supplementary water to be backwashed to the water tank 2 being provided with electrolysis unit 3 by impurity (implying that electrolyte), and it can in order to provide electrolysis unit 3 to carry out the electrolysis water needed for electrolysis. Further, the electrolysis water 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, electrolysis water W required during to provide electrolysis unit 3 electrolysis.

Comprehensive, the focusing on of the present invention proposes a kind of gas generator, and it comprises electrolysis unit and humidification device. In the gas generator of the present invention, hydrogen and oxygen gas mixture produced by electrolysis unit can carry out humidifying by humidification device, with the hydrogen and oxygen gas mixture providing applicable human body to suck. Additionally, hydrogen and oxygen gas mixture produced by electrolysis unit can pass through humidification device, to produce to dissolve the hydrogen water of the hydrogen and oxygen gas mixture of higher concentration, when practical application, visual user is required to produce the hydrogen water with the hydrogen and oxygen gas mixture of desired concn. Additionally, by the present invention be designed in order to supplement supplement water, electrolyte is backwashed to electrolysis unit, in order to recover the filter capacity of circulatory flow, the obstruction preventing circulatory flow and corrosion and to lower electrolytical consumption simultaneously.

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 of the gas generator illustrating present invention different visual angles in the 15th specific embodiment, Figure 19 is the gas generator illustrating present invention rearview in embodiment shown in Figure 18 A, and Figure 20 A and Figure 20 B is the top view illustrating and only having condensate filter and water tank lid in Figure 18 A illustrated embodiment and the line D-D along this top view cuts open the profile set. In the 15th specific embodiment, the gas generator of the present invention comprises water tank, electrolysis unit, atomization/volatilization gas mixing channel, pumping plant, condensate filter, chiller and humidification device. Owing to the structural design of said elements is in explanation made 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 is only consisted of the effect that can reach condensation two groups of runner 640a, and the design simplification of condensate filter 6 and cost can be made to reduce simultaneously. Additionally, 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 so that it is become a modular design, and it can save space more compared to the design of the 14th specific embodiment simultaneously. In addition, when modular water tank 2, pumping plant 5, condensate filter 6 and chiller 7 assemble with atomization/volatilization gas mixing channel 4 and humidification device 9, the present invention can have easy to assembly and pipeline simplification advantage, so that the global design of the gas generator of the present invention optimizes more.

In an embodiment, when electrolysis unit electrically connects with external power source, the output voltage of power supply is about between 17 volts (V) to 27 volts (V), the output electric 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 of electrode (between both positive and negative polarity) is between 3 volts (V), is between 12V��24V if any eight groups of voltages then used. But it is not limited, when practical application, when electrolysis unit electrically connects with external power source, the output voltage of power supply is about between 5 volts (V) to 24 volts (V), the output electric 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.

In sum, the present invention proposes a kind of gas generator, and it comprises electrolysis unit and condensate filter. In the gas generator of the present invention, hydrogen and oxygen gas mixture produced by electrolysis unit can be undertaken condensing and filter impurity therein by condensate filter, to provide one to be suitable for the hydrogen and oxygen gas mixture that human body sucks. Meanwhile, it is designed to while supplementary water to backwash electrolyte to electrolysis unit by the present invention, in order to reduce electrolytical consumption and to avoid electrolyte to block in condensate filter.

By the above detailed description of preferred embodiments, it is intended to clearly describe inventive feature and spirit, and not with above-mentioned disclosed preferred embodiment, scope of the invention is any limitation as. On the contrary, its objective is that the present invention that is arranged in wishing to contain various change and tool equality is intended in the category of the scope of the claims of application. Although the present invention is disclosed above with embodiment; so it is not limited to the present invention; any it is 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, therefore protection scope of the present invention ought be as the criterion depending on the scope that appending claims defines.

Claims

1. a gas generator, it is characterised in that comprise:

One electrolysis unit, an accommodating electrolysis water, this electrolysis unit in order to this electrolysis water of electrolysis to produce a hydrogen and oxygen gas mixture; And

One condensate filter, in order to condense this hydrogen and oxygen gas mixture the impurity filtering in this hydrogen and oxygen gas mixture, this condensate filter has a blowhole and a venthole, and this blowhole is in order to receive this hydrogen and oxygen gas mixture, and this venthole is in order to discharge this hydrogen and oxygen gas mixture after filtration;

Wherein this venthole of this condensate filter can be used to input a benefit and is filled with water to this electrolysis unit.

2. gas generator according to claim 1, it is characterized in that, this condensate filter includes multiple condensate film, each condensate film has a runner, this runner of this condensate film is interconnected with this runner of this adjacent condensate film, so as to forming the circulatory flow for the circulation of this hydrogen and oxygen gas mixture.

3. gas generator according to claim 2, it is characterized in that, this runner is formed by a gradual-enlargement type runner and a connection runner, and this gradual-enlargement type runner of this condensate film passes through this connection runner of this condensate film to be interconnected with this gradual-enlargement type runner of this adjacent condensate film.

4. gas generator according to claim 3, it is characterized in that, this gradual-enlargement type runner is the runner of a cross section flaring, this gradual-enlargement type runner comprises an opening, this connection runner has a runner and two corresponding openings, this two corresponding opening of this connection runner is by this runner to be interconnected, and this opening of this gradual-enlargement type runner of this condensate film passes through this two corresponding opening of this connection runner of this condensate film to be interconnected with this opening of this gradual-enlargement type runner of this adjacent condensate film.

5. gas generator according to claim 2, it is characterised in that this circulatory flow is to be communicated between this blowhole and this venthole.

6. gas generator according to claim 2, it is characterised in that this runner is provided with an activated carbon fiber, in order to filter this impurity in this hydrogen and oxygen gas mixture.

7. gas generator according to claim 6, it is characterised in that this runner is separately provided with arbitrary filtering material being made up of pottery, quartz, kieselguhr, meerschaum or combination of the above.

8. gas generator according to claim 1, it is characterised in that this impurity is the electrolyte in this electrolysis water.

9. gas generator according to claim 8, it is characterised in that this impurity is sodium hydroxide.

10. gas generator according to claim 1, it is characterized in that, this gas generator separately includes a water tank, this water tank has one first hollow bulb and a conduit, this electrolysis unit is disposed within this first hollow bulb of this water tank, this conduit is connected to this blowhole of this condensate filter, in order to export this hydrogen and oxygen gas mixture to this condensate filter.

11. gas generator according to claim 10, it is characterized in that, when this electrolysis unit suspends this electrolysis water of electrolysis to produce this hydrogen and oxygen gas mixture, this venthole of this condensate filter can be used to input this supplementary water, and this impurity can also be backwashed to this electrolysis unit and this first hollow bulb via this blowhole and this conduit by this supplementary water.

12. gas generator according to claim 1, it is characterised 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..

13. gas generator according to claim 1, it is characterized in that, separately comprise one atomization/volatilization gas mixing channel, wherein this atomization/volatilization gas mixing channel connects this venthole of this condensate filter, to receive this hydrogen and oxygen gas mixture after filtering, wherein this atomization/volatilization gas mixing channel produce an atomization gas and filter after this hydrogen and oxygen gas mixture mix, to form a health care gas for the suction of this user, wherein this atomization gas is selected from by water vapour, atomization liquid medicine, volatile spirits and combination, the one in the group formed.

14. gas generator according to claim 1, it is characterised in that this impurity can be backwashed to this electrolysis unit via this blowhole by this supplementary water.

15. gas generator according to claim 1, it is characterised in that when this electrolysis unit suspends this electrolysis water of electrolysis to produce this hydrogen and oxygen gas mixture, this impurity can be backwashed to this electrolysis unit via this blowhole by this supplementary water.