CN106082123B - Aqueous medium fuel produce and burner - Google Patents
Aqueous medium fuel produce and burner Download PDFInfo
- Publication number
- CN106082123B CN106082123B CN201610662384.2A CN201610662384A CN106082123B CN 106082123 B CN106082123 B CN 106082123B CN 201610662384 A CN201610662384 A CN 201610662384A CN 106082123 B CN106082123 B CN 106082123B
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- Prior art keywords
- burner
- catalysis
- catalysis electrode
- cover plate
- tubular pole
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
- C01B3/04—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by decomposition of inorganic compounds, e.g. ammonia
- C01B3/042—Decomposition of water
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23K—FEEDING FUEL TO COMBUSTION APPARATUS
- F23K5/00—Feeding or distributing other fuel to combustion apparatus
- F23K5/002—Gaseous fuel
-
- 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
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Inorganic Chemistry (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
Abstract
A kind of aqueous medium fuel produce and burner, it is related to burner apparatus, including pressure pump, pressurized tank, burner and electrostatic generator, the delivery port of pressure pump is attached by the bottom of check-valves and pressurized tank, burner assembly is by catalysis electrode, tubular pole seat and cover plate composition, there is water guide duct in the body of catalysis electrode, more catalysis electrodes are arranged on the screw socket of tubular pole seat, water guide duct in catalysis electrode body connects with space in the pipe of tubular pole seat, space forms pressure-bearing hydroecium in the pipe of tubular pole seat, cover plate is arranged on by insulated support on the body of tubular pole seat, the micropore cone of catalysis electrode upper semisection is placed among the duct of cover plate；The anode interface of catalysis electrode and electrostatic generator is electrically connected, and the negative pole interface of cover plate and electrostatic generator is electrically connected.The present invention is using aqueous medium as gasified raw material, and water by pressure permeation, catalysis and ionization, the vaporising fuel for being decomposed into hydrogen-oxygen is burnt.
Description
Technical field
The present invention relates to burner apparatus, especially relates to a kind of aqueous medium combustion apparatus.
Background technology
Water is a kind of material most abundant containing protium, and each hydrone is by two hydrogen atoms and an oxygen atom knot
Conjunction forms, and containing the hydrogen more than 111 kilograms in every cubic meter of water, its quality capacity is more than 11.1%, and the calorific capacity of hydrogen is high, combustion
142120kj heat can be released by burning 1 kg hydrogen, be three times of gasoline.Water is developed into a kind of energy and applied, during burning
Carbon dioxide is not produced, product only has water, can be repeatedly circulated, and to improving air acid rain environment, reduces dioxy in air
Change carbon content, have great benefit so as to mitigate greenhouse effects.Therefore, exploitation aqueous medium fuel can not only solve energy shortage
Situation, and environment protecting protrude.However, the hydrogen atom and oxygen atom in hydrone combine very firm, high-temperature heating
Method need to be heated to hydrone to be decomposed for more than 3000 DEG C, and in general mode of heating is difficult to reach so high temperature；Industry
On with current method decompose hydrone hydrogen manufacturing, decomposition rate is slow, efficiency is low, and consume energy it is very big.
The content of the invention
The shortcomings that the invention aims to overcome existing pyrolysis water hydrogen manufacturing and current method to decompose hydrone hydrogen manufacturing, there is provided one
Kind of aqueous medium fuel produce and burner, applied using water as a kind of energy, realize cleaning burning, protecting ecology ring
Border.
A kind of aqueous medium fuel of the present invention produce and burner, including pressure pump, pressurized tank, burner and quiet
Electric generator, the delivery port of pressure pump is attached by the bottom of check-valves and pressurized tank, it is characterized in that burner assembly 1
It is made up of catalysis electrode 1-4, tubular pole seat 1-7 and cover plate 1-1, wherein, catalysis electrode 1-4 is more than one, catalysis electrode
1-4 upper semisection is micropore conical structure, has water guide duct 1-401 in catalysis electrode 1-4 lower half segment body；Tubular pole seat
1-7 is the hollow circular-tube structure of endcapped, has a row to be used for the screw socket 1-3 for installing catalysis electrode on tubular pole seat 1-7；
There is the duct 1-2 of quantity identical with catalysis electrode on cover plate 1-1；More catalysis electrode 1-4 are arranged on tubular pole seat 1-7 spiral shell
On mouth 1-3, the water guide duct 1-401 in catalysis electrode 1-4 bodies connects with space in tubular pole seat 1-7 pipe, in tubular type electricity
Electrode seat 1-7 front end has water supply connector 21 to access, and space forms pressure-bearing hydroecium 20 in tubular pole seat 1-7 pipe；Cover plate 1-1 leads to
Insulated support 1-6 is crossed on tubular pole seat 1-7 body, the micropore cone of catalysis electrode 1-4 upper semisections is placed in
Among cover plate 1-1 duct 1-2；Catalysis electrode 1-4 passes through tubular pole seat 1-7 metal wall and the positive pole of electrostatic generator
Interface is electrically connected, and the negative pole interface of cover plate 1-1 and electrostatic generator is electrically connected；On tubular pole seat 1-7
Water supply connector 21 is connected on the pipeline between check-valves 12 and pressurized tank 16.
In the present invention, catalysis electrode 1-4 is metal powder sintered miillpore filter structure, and catalysis electrode 1-4 forms moisture
Son filtering and catalysis element, sintered into when it is implemented, catalysis electrode 1-4 is the material that tungsten powder and nickel-sulfur alloy powder mix
Tungsten nickel pseudo-alloy part, during firing, the neither mutual phased soln of tungsten, nickel-sulfur alloy, intermetallic compound is not also formed, the vacation formed
Alloy structure is tungsten particle, two phase structures of nickel-sulfur alloy particle, micro-pore in pseudo-alloy tissue be present, and micro-pore is formed
The filtration channel of hydrone, have the function that to filter hydrone, there is catalysis to make for decomposition of the nickel-sulfur alloy therein to hydrone
With, make hydrone be easier decompose；There are space, catalysis electrode 1-4 between catalysis electrode 1-4 and cover plate 1-1 duct 1-2 wall bodies
Space between cover plate 1-1 duct 1-2 wall bodies forms electrostatic field；There is normally closed air bleeding valve in tubular pole seat 1-7 tail end
2, normally closed air bleeding valve 2 is communicated to space in tubular pole seat 1-7 pipe；Duct 1-2 on cover plate 1-1 is the up-small and down-big loudspeaker that falls
Shape structure；Breathing interface 16-1 is arranged at the bottom of pressurized tank, and the delivery port of pressure pump passes through check-valves 12 and pressure pot bottom
Breathing interface 16-1 be attached；There is filter 10 on the pipeline that pressure pump 8 accesses；Burner assembly 1 be one with
On, when burner assembly 1 is multiple, the pipe interface between check-valves 12 and pressurized tank 16 is connected to each combustion by water knockout drum
In the water supply connector of burner component, the catalysis electrode of each burner assembly is entered with the anode interface of parallel way and electrostatic generator
Row electrical connection, the cover plate of each burner assembly are electrically connected with the negative pole interface of parallel way and electrostatic generator.
The present invention is adapted to apply on Industrial Boiler, using aqueous medium as gasified raw material, realizes cleaning burning, obtains heat energy,
Using when, pressure pump, pressurized tank, electrostatic generator and burner assembly 1 be arranged on respective frame on.During work, to urging
Apply more than 10,000 volts of electrostatic between polarizing electrode 1-4 and cover plate 1-1, be in the micropore cone of catalysis electrode 1-4 upper semisections
In electrostatic field among the 1-2 of duct, to increase catalysis electrode 1-4 catalytic activity, and ionization is formed to hydrone；Adopt
By the use of pure water as raw water, the pressurized water pump 8 of raw water is entered in the pressure-bearing hydroecium 20 of burner assembly 1, while raw material
Water is entered in pressurized tank by the breathing interface 16-1 of the bottom of pressurized tank 16, is compressed the upper air in pressurized tank 16, shape
Into compressed air, the water of the bottom of pressurized tank 16 has pressure in the presence of compressed air, hydraulic pressure and pressure in pressure-bearing hydroecium 20
The hydraulic pressure of the bottom of power tank 16 is equal.The pure water with pressure penetrates into catalysis by water guide duct 1-401 in pressure-bearing hydroecium 20
In electrode 1-4 micro-pore, catalysis electrode 1-4 micro-pore filters to hydrone, macromolecular mass is turned into small point
Son, the activity of hydrone are improved, and make hydrone be easier to be decomposed, meanwhile, catalysis electrode 1-4 nickel-sulfur alloy material
Hydrone is catalytically decomposed.Hydrone is changed into small molecular cluster structure by pressure permeation by macromolecular mass, then through nickel
Sulphur alloy material is catalyzed and electrostatic field ionization, is decomposed into hydrogen, oxygen and active hydrogen atom, active oxygen atom, active hydrogen-oxygen
The activity chemistry thing of atomic group, escaped from the micropore cone of catalysis electrode 1-4 upper semisections, turn into vaporising fuel, enter
In the 1-2 of duct, the vaporising fuel of hydrone conversion is carried out by the high-voltage spark between catalysis electrode 1-4 and duct 1-2 wall bodies
Light, carry out back reaction burning, release heat energy.In said process, the water of water and infiltration catalysis electrode 1-4 in pressure-bearing hydroecium 20
Cooling effect is produced to catalysis electrode 1-4, protects catalysis electrode 1-4 not to be burned.The present invention improves catalysis electricity using electrostatic
Pole 1-4 catalytic activity and hydrone is ionized using electrostatic field, reduce the temperature requirement of pyrolysis hydrone, institute's consuming electric power pole
Few, the decomposition efficiency of hydrone is high.
The beneficial effects of the invention are as follows：The aqueous medium fuel of offer produce and burner, be adapted on Industrial Boiler
Using, using aqueous medium as gasified raw material, hydrone by pressure permeation, small molecular cluster structure is changed into by macromolecular mass, then
Through the catalysis of nickel-sulfur alloy material and electrostatic field ionization, the vaporising fuel for being decomposed into hydrogen-oxygen is burnt, using water as a kind of energy
To apply, cleaning burning is realized, is preserved the ecological environment.
Brief description of the drawings
Fig. 1 be the present invention aqueous medium fuel produce and burner structure chart.
Fig. 2 is the enlarged drawing of the catalysis electrode of the present invention.
In figure：1. burner assembly, 1-1. cover plates, 1-2. ducts, 1-3. screw sockets, 1-4. catalysis electrodes, 1-401. water guides
Duct, 1-402. external screw threads, 1-403. outer-hexagonal bodies, 1-404. micropore cones, 1-5. positioning screws, 1-6. insulating supportings
Part, 1-7. tubular pole seats, 1-8. water inlet interfaces, 2. normally closed air bleeding valves, 3. return lines, 4. insulating supports, 5. high-voltage lines, 6. is quiet
Electric generator, 6-1. negative pole interfaces, 6-2. anode interfaces, 7. penstocks, 8. pressure pumps, 9. communicating pipes, 10. filters,
11. feed pipe, 12. check-valves, 13. threeways, 14. frames, 15. pressure pure water, 16. pressurized tanks, 16-1. breathing interfaces, 16-
2. satellite interface, 16-3. maintenance evacuated tubes, 17. compressed airs, 18. pressure controllers, 19. maintenance exhaust-valves, 20. artesian waters
Room, 21. water supply connectors.
Embodiment
In embodiment shown in the Fig. 1 of embodiment 1, aqueous medium fuel produce and burner is mainly by pressure pump
8th, pressurized tank 16, burner assembly 1 and electrostatic generator 6 form, and the delivery port of pressure pump 8 passes through check-valves 12 and pressurized tank
The breathing interface 16-1 of bottom is attached, and burner assembly 1 includes catalysis electrode 1-4, tubular pole seat 1-7 and cover plate 1-1,
Wherein, catalysis electrode 1-4 is more than one, and catalysis electrode 1-4 upper semisection is micropore conical structure, catalysis electrode 1-4's
There is water guide duct 1-401 in lower half segment body；Tubular pole seat 1-7 is the hollow circular-tube structure of endcapped, in tubular pole seat
There is a row to be used for the screw socket 1-3 for installing catalysis electrode on 1-7；There is the duct 1-2 of quantity identical with catalysis electrode on cover plate 1-1；
More catalysis electrode 1-4 are on tubular pole seat 1-7 screw socket 1-3, the water guide duct 1-401 in catalysis electrode 1-4 bodies
Connected with space in tubular pole seat 1-7 pipe, there is water supply connector 21 to access in tubular pole seat 1-7 front end, tubular pole
Space forms pressure-bearing hydroecium 20 in seat 1-7 pipe；Cover plate 1-1 is arranged on tubular pole seat 1-7 pipe by insulated support 1-6
On body, the micropore cone of catalysis electrode 1-4 upper semisections is placed among cover plate 1-1 duct 1-2, catalysis electrode 1-4 and duct
There is space between 1-2 wall bodies；Catalysis electrode 1-4 is connect by tubular pole seat 1-7 metal wall and the positive pole of electrostatic generator
Mouth is electrically connected, and the negative pole interface of cover plate 1-1 and electrostatic generator is electrically connected, catalysis electrode 1-4 and cover plate 1-1
Duct 1-2 wall bodies between space form electrostatic field；Water supply connector 21 on tubular pole seat 1-7 be connected to check-valves 12 with
On pipeline between pressurized tank 16.In the present embodiment, catalysis electrode 1-4 is metal powder sintered miillpore filter structure, catalysis
Electrode 1-4 forms hydrone filtering and catalysis element, and catalysis electrode 1-4 is that the material that tungsten powder and nickel-sulfur alloy powder mix burns
Form tungsten nickel pseudo-alloy part, during firing, the neither mutual phased soln of tungsten, nickel-sulfur alloy, also do not form intermetallic compound, formed
Pseudo-alloy be organized as two phase structures of tungsten particle, nickel-sulfur alloy particle, micro-pore, micro-pore be present in pseudo-alloy tissue
The filtration channel of hydrone is formed, has the function that to filter hydrone, decomposition of the nickel-sulfur alloy therein to hydrone, which has, urges
Change acts on, and makes hydrone be easier to decompose；There is normally closed air bleeding valve 2 in tubular pole seat 1-7 tail end, normally closed air bleeding valve 2 connects
To space in tubular pole seat 1-7 pipe, for the first time in use, opening normally closed air bleeding valve 2, the air in pressure-bearing hydroecium 20 is with water inlet
And discharge, it is easy into water to make；Duct 1-2 on cover plate 1-1 is up-small and down-big inverted tubaeform structure；Accessed in pressure pump 8
Pipeline on have filter 10；There are pressure controller 18 and maintenance exhaust-valve 19 on the top of pressurized tank 16 or top.
The present embodiment uses in Industrial Boiler, and burner assembly 1 is arranged on the insulating support 4 in industrial boiler furnace
On, ground protection processing is carried out to cover plate 1-1, pressure pump 8, pressurized tank 16 and electrostatic generator 6 are arranged on Industrial Boiler
Periphery.During work, the electrostatic to applying more than 10,000 volts between catalysis electrode 1-4 and cover plate 1-1, make catalysis electrode 1-4 upper semisections
Micropore cone be in the electrostatic field among the 1-2 of duct, to increase catalysis electrode 1-4 catalytic activity, and to moisture
Son forms ionization；The pressure-bearing of burner assembly 1 is entered as raw water, the pressurized water pump 8 of raw water using pure water
In hydroecium 20, while raw water is entered in pressurized tank by the breathing interface 16-1 of the bottom of pressurized tank 16, is made upper in pressurized tank 16
Portion's air is compressed, and forms compressed air, and the water of the bottom of pressurized tank 16 has pressure, artesian water in the presence of compressed air
Hydraulic pressure in room 20 is equal with the hydraulic pressure of the bottom of pressurized tank 16.The pure water with pressure passes through water guide duct in pressure-bearing hydroecium 20
1-401 is penetrated into catalysis electrode 1-4 micro-pore, and catalysis electrode 1-4 micro-pore filters to hydrone, is made big
Micel turns into small molecule, and the activity of hydrone is improved, and makes hydrone be easier to be decomposed, meanwhile, catalysis electrode 1-4
Nickel-sulfur alloy material hydrone is catalytically decomposed.Hydrone is changed into small point by pressure permeation by macromolecular mass
Sub- unity structure, then through the catalysis of nickel-sulfur alloy material and electrostatic field ionization, it is decomposed into hydrogen, oxygen and active hydrogen atom, activity
The activity chemistry thing of oxygen atom, reactive hydrogen oxygen atomic group, escape, turn into from the micropore cone of catalysis electrode 1-4 upper semisections
Vaporising fuel, enter in the 1-2 of duct, the vaporising fuel of hydrone conversion is by between catalysis electrode 1-4 and duct 1-2 wall bodies
High-voltage spark is lighted, and carries out back reaction burning, releases heat energy.In the above-mentioned course of work, the operation pressure in pressurized tank 16
Power is controlled by pressure controller 18, and when threshold pression of the pressure in pressurized tank 16 less than setting, pressure controller 18 connects
The power supply of logical pressure pump 8, runs pressure pump 8, and moisturizing is carried out to pressurized tank 16, make the air in pressurized tank 16 compress and
Raise pressure inside the tank；When the pressure in pressurized tank 16 reaches the pressure upper limit of setting, pressure controller 18 disconnects pressure (hydraulic) water
The power supply of pump 8, stop pressure pump 8, by the control of pressure controller 18, make the pressure in pressurized tank 16 in the model of setting
It is constant to enclose interior holding.
The aqueous medium fuel of embodiment 2 produce and burner mainly by pressure pump 8, pressurized tank 16, electrostatic occur
Device 6 and three burner assembly compositions, the pipe interface between check-valves 12 and pressurized tank 16 are connected to three by water knockout drum
In the water supply connector of burner assembly, the catalysis electrode of three burner assemblies is connect with the positive pole of parallel way and electrostatic generator
Mouth is electrically connected, and the cover plate of each burner assembly is electrically connected with the negative pole interface of parallel way and electrostatic generator
Connect.Other structures are basically the same as those in the first embodiment, and repeat no more.
Claims (8)
1. a kind of aqueous medium fuel produce and burner, including pressure pump, pressurized tank, burner and electrostatic generator,
The delivery port of pressure pump is attached by the bottom of check-valves and pressurized tank, it is characterized in that burner assembly（1）By being catalyzed
Electrode（1-4）, tubular pole seat（1-7）And cover plate（1-1）Composition, wherein, catalysis electrode（1-4）For more than one, catalysis electricity
Pole（1-4）Upper semisection be micropore conical structure, catalysis electrode（1-4）Lower half segment body in have water guide duct（1-401）；Pipe
Formula electrode tip holder（1-7）For the hollow circular-tube structure of endcapped, in tubular pole seat（1-7）On have a row be used for install catalysis it is electric
The screw socket of pole（1-3）；Cover plate（1-1）On have the duct of quantity identical with catalysis electrode（1-2）；Catalysis electrode（1-4）It is arranged on
Tubular pole seat（1-7）Screw socket（1-3）On, catalysis electrode（1-4）Water guide duct in body（1-401）With tubular pole seat
（1-7）Pipe in space connection, in tubular pole seat（1-7）Front end have water supply connector（21）Access, tubular pole seat（1-7）
Pipe in space form pressure-bearing hydroecium（20）；Cover plate（1-1）Pass through insulated support（1-6）Installed in tubular pole seat（1-7）
Body on, catalysis electrode（1-4）The micropore cone of upper semisection is placed in cover plate（1-1）Duct（1-2）Among；Catalysis electrode
（1-4）Pass through tubular pole seat（1-7）Metal wall and the anode interface of electrostatic generator be electrically connected, cover plate（1-
1）It is electrically connected with the negative pole interface of electrostatic generator；Tubular pole seat（1-7）On water supply connector（21）It is connected to only
Return valve（12）With pressurized tank（16）Between pipeline on.
2. a kind of aqueous medium fuel according to claim 1 produce and burner, it is characterized in that catalysis electrode（1-4）
For metal powder sintered miillpore filter structure, catalysis electrode（1-4）Form hydrone filtering and catalysis element.
3. a kind of aqueous medium fuel according to claim 1 produce and burner, it is characterized in that catalysis electrode（1-4）
With cover plate（1-1）Duct（1-2）There are space, catalysis electrode between wall body（1-4）With cover plate（1-1）Duct（1-2）Wall body
Between space form electrostatic field.
4. a kind of aqueous medium fuel according to claim 1 produce and burner, it is characterized in that in tubular pole seat
（1-7）Tail end have normally closed air bleeding valve（2）, normally closed air bleeding valve（2）It is communicated to tubular pole seat（1-7）Pipe in space.
5. a kind of aqueous medium fuel according to claim 1 produce and burner, it is characterized in that cover plate（1-1）On
Duct（1-2）For up-small and down-big inverted tubaeform structure.
6. a kind of aqueous medium fuel according to claim 1 produce and burner, it is characterized in that the bottom of pressurized tank
There is breathing interface（16-1）, the delivery port of pressure pump passes through check-valves（12）With the breathing interface of pressure pot bottom（16-1）Enter
Row connection.
7. a kind of aqueous medium fuel according to claim 1 produce and burner, it is characterized in that in pressure pump（8）
There is filter on the pipeline of access（10）.
8. a kind of aqueous medium fuel according to claim 1 produce and burner, it is characterized in that burner assembly（1）
For more than one, work as burner assembly（1）For it is multiple when, check-valves（12）With pressurized tank（16）Between pipe interface by point
Hydrophone is connected in the water supply connector of each burner assembly, and the catalysis electrode of each burner assembly is occurred with parallel way and electrostatic
The anode interface of device is electrically connected, and the cover plate of each burner assembly is entered with the negative pole interface of parallel way and electrostatic generator
Row electrical connection.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610662384.2A CN106082123B (en) | 2016-08-15 | 2016-08-15 | Aqueous medium fuel produce and burner |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610662384.2A CN106082123B (en) | 2016-08-15 | 2016-08-15 | Aqueous medium fuel produce and burner |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN106082123A CN106082123A (en) | 2016-11-09 |
| CN106082123B true CN106082123B (en) | 2018-04-03 |
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ID=57456286
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610662384.2A Active CN106082123B (en) | 2016-08-15 | 2016-08-15 | Aqueous medium fuel produce and burner |
Country Status (1)
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Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201372312Y (en) * | 2008-12-18 | 2009-12-30 | 白玉林 | Aqueous oxy-hydrogen source integrated extraction multi-purposed machine unit |
| CN101749742A (en) * | 2008-12-05 | 2010-06-23 | 黄富成 | A hydrogen-oxygen combustion burner |
| CN103175229A (en) * | 2006-05-01 | 2013-06-26 | Gbd公司 | Method for utilizing combustible gas produced by electrolytic cell to cook and equipment |
| CN105402779A (en) * | 2015-12-23 | 2016-03-16 | 金烜伊 | Gas stove with water electrolysis assisting in combustion |
| CN205990231U (en) * | 2016-08-15 | 2017-03-01 | 衢州昀睿工业设计有限公司 | The producing and burner of aqueous medium fuel |
-
2016
- 2016-08-15 CN CN201610662384.2A patent/CN106082123B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103175229A (en) * | 2006-05-01 | 2013-06-26 | Gbd公司 | Method for utilizing combustible gas produced by electrolytic cell to cook and equipment |
| CN101749742A (en) * | 2008-12-05 | 2010-06-23 | 黄富成 | A hydrogen-oxygen combustion burner |
| CN201372312Y (en) * | 2008-12-18 | 2009-12-30 | 白玉林 | Aqueous oxy-hydrogen source integrated extraction multi-purposed machine unit |
| CN105402779A (en) * | 2015-12-23 | 2016-03-16 | 金烜伊 | Gas stove with water electrolysis assisting in combustion |
| CN205990231U (en) * | 2016-08-15 | 2017-03-01 | 衢州昀睿工业设计有限公司 | The producing and burner of aqueous medium fuel |
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| Publication number | Publication date |
|---|---|
| CN106082123A (en) | 2016-11-09 |
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