CN106145032B - Aqueous medium gasified combustion apparatus - Google Patents
Aqueous medium gasified combustion apparatus Download PDFInfo
- Publication number
- CN106145032B CN106145032B CN201610662402.7A CN201610662402A CN106145032B CN 106145032 B CN106145032 B CN 106145032B CN 201610662402 A CN201610662402 A CN 201610662402A CN 106145032 B CN106145032 B CN 106145032B
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- electrode
- disk
- duct
- catalysis
- catalysis electrode
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Classifications
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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
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
Abstract
A kind of aqueous medium gasified combustion apparatus, it is related to burner apparatus, burner assembly takes up disk, duct cover disk and insulated chassis by catalysis electrode, electrode and formed, and electrode takes up the mounting hole for having catalysis electrode on disk, there is the duct of quantity identical with catalysis electrode on the cover disk of duct, it is fluted in insulated chassis；Catalysis electrode and duct cover disk are taken up on disk installed in electrode, the micropore cone of catalysis electrode upper semisection is placed among the duct of duct cover disk, electrode takes up disk on insulated chassis and is enclosed in groove port, and space forms pressure-bearing hydroecium in the groove of insulated chassis；The anode interface and negative pole interface of electrostatic generator are electrically connected with catalysis electrode, duct cover disk respectively, and the water supply connector of pressure-bearing hydroecium is connected on the pipeline between check-valves and pressurized tank.The present invention is adapted to apply on Industrial Boiler, water by pressure permeation, then through the catalysis of nickel-sulfur alloy material and electrostatic field ionization, is decomposed into hydrogen, oxygen activity chemicals are 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 aqueous medium gasified combustion apparatus, is applied using water as a kind of energy, is realized cleaning burning, is preserved the ecological environment.
A kind of aqueous medium gasified combustion apparatus of the present invention, including pressure pump, pressurized tank, burner and electrostatic occur
Device, 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 is by being catalyzed
Electrode 1-4, electrode take up disk 1-1, duct cover disk 1-2 and insulated chassis 1-9 composition, wherein, catalysis electrode 1-4 forms hydrone
Filtering and catalysis element, catalysis electrode 1-4 upper semisection is in micropore conical structure, is had in catalysis electrode 1-4 lower half segment body
Water guide duct 1-401, catalysis electrode 1-4 are more than one；Electrode takes up the mounting hole for having catalysis electrode 1-4 on disk 1-1；Duct
There is the duct 1-3 of quantity identical with catalysis electrode 1-4 on cover disk 1-2；It is fluted in insulated chassis 1-9；Catalysis electrode 1-4 and hole
Road cover disk 1-2 is taken up on disk 1-1 installed in electrode, and the micropore cone of catalysis electrode 1-4 upper semisections is placed in duct cover disk 1-2's
Among the 1-3 of duct, the space between catalysis electrode 1-4 and duct 1-3 wall body forms electrostatic field；Electrode takes up disk 1-1 installations
On insulated chassis 1-9 and it is enclosed in groove port, space forms pressure-bearing hydroecium 18, catalysis electricity in insulated chassis 1-9 groove
Pole 1-4 water guide duct 1-401 is communicated to pressure-bearing hydroecium 18, and pressure-bearing hydroecium 18 has water supply connector 1-8 accesses；Electrostatic generator
Anode interface and negative pole interface are electrically connected with catalysis electrode 1-4, duct cover disk 1-2 respectively, the water inlet of pressure-bearing hydroecium 18
Joint 1-8 is connected on the pipeline between check-valves 10 and pressurized tank 14.During concrete application, at the top of pressurized tank 14 or top
There are pressure controller 16 and maintenance exhaust-valve 17.
In the present invention, catalysis electrode 1-4 is metal powder sintered miillpore filter structure, and the micropore between metal dust is formed
The filtration channel of hydrone, when it is implemented, the material that catalysis electrode 1-4 is mixed from tungsten powder and nickel-sulfur alloy powder, 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 be present in pseudo-alloy tissue, there is filtering
The effect of hydrone, decomposition of the nickel-sulfur alloy therein to hydrone have catalytic action, make hydrone be easier to decompose；In electricity
Pole, which takes up, metal backing 1-5 on the inside of disk 1-1, metal backing 1-5 is connected to catalysis electrode 1-4, has on metal backing 1-5
Conductive plug 1-6, there is an electrically conductive socket 1-7 on insulated chassis 1-9, and during assembling, the conductive plug 1-6 on metal backing 1-5 is inserted
Enter into the electrically conductive socket 1-7 on insulated chassis 1-9, the positive pole that electrically conductive socket 1-7 is wired to electrostatic generator 4 connects
On mouth 4-2；Being taken up in electrode on disk 1-1 has normally closed air bleeding valve 20, and normally closed air bleeding valve 20 is communicated to pressure-bearing hydroecium 18；Duct cover disk
Duct 1-3 on 1-2 is up-small and down-big inverted tubaeform structure；Breathing interface 14-1 is arranged at the bottom of pressurized tank, pressure pump
Delivery port is attached by the breathing interface 14-1 of check-valves 10 and pressure pot bottom；On the pipeline that pressure pump 6 accesses
There is filter 8.
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
Polarizing electrode 1-4 and duct cover disk 1-2 applies more than 10,000 volts of electrostatic, is in catalysis electrode 1-4 upper semisection micropore cone
In electrostatic field among the 1-3 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 6 of raw water is entered in the pressure-bearing hydroecium 18 of burner assembly 1, while raw material
Water is entered in pressurized tank by the bottom of pressurized tank 14, is compressed the upper air in pressurized tank 14, forms compressed air, pressure
The water of the bottom of power tank 14 has pressure in the presence of compressed air, the hydraulic pressure in pressure-bearing hydroecium 18 and the water of the bottom of pressurized tank 14
Press equal.The pure water with pressure penetrates into catalysis electrode 1-4 micro hole by water guide duct 1-401 in pressure-bearing hydroecium 18
In gap, catalysis electrode 1-4 micro-pore filters to hydrone, macromolecular mass is turned into small molecule, the activity of hydrone
It is improved, makes hydrone be easier to be decomposed, meanwhile, catalysis electrode 1-4 nickel-sulfur alloy material is urged hydrone
Change and decompose.Hydrone is changed into small molecular cluster structure, then be catalyzed through nickel-sulfur alloy material by pressure permeation by macromolecular mass
With electrostatic field ionization, the activation of hydrogen, oxygen and active hydrogen atom, active oxygen atom, reactive hydrogen oxygen atomic group is decomposed into
Thing is learned, is escaped from catalysis electrode 1-4 upper semisection micropore cone, is turned into vaporising fuel, enter in the 1-3 of duct, moisture
The vaporising fuel of son conversion is lighted by the high-voltage spark between catalysis electrode 1-4 and duct 1-3 wall bodies, carries out back reaction
Burning, release heat energy.In said process, the water of water and infiltration catalysis electrode 1-4 in pressure-bearing hydroecium 18 produces to catalysis electrode 1-4
Raw cooling effect, protects catalysis electrode 1-4 not to be burned.The present invention improves catalysis electrode 1-4 catalytic activity using electrostatic
Hydrone is ionized with using electrostatic field, reduces the temperature requirement of pyrolysis hydrone, institute's consuming electric power is few, the decomposition of hydrone
Efficiency high.
The beneficial effects of the invention are as follows：A kind of aqueous medium gasified combustion apparatus provided, is adapted to apply on Industrial Boiler,
Using aqueous medium as gasified raw material, hydrone by pressure permeation, small molecular cluster structure is changed into by macromolecular mass, then through nickel sulphur
Alloy material is catalyzed and electrostatic field ionization, the vaporising fuel for being decomposed into hydrogen-oxygen are burnt, applied using water as a kind of energy,
Cleaning burning is realized, is preserved the ecological environment.
Brief description of the drawings
Fig. 1 is a kind of structure chart of aqueous medium gasified combustion apparatus of the present invention.
Fig. 2 is the attached view of burner assembly of the present invention.
Fig. 3 is the enlarged drawing of the catalysis electrode of the present invention.
In figure：1. burner assembly, 1-1. electrodes take up disk, 1-2. ducts cover disk, 1-3. ducts, 1-4. catalysis electrodes,
1-401. water guides duct, 1-402. outer-hexagonal bodies, 1-403. external screw threads, 1-404. micropore cones, 1-5. metal backings, 1-6.
Conductive plug, 1-7. electrically conductive sockets, 1-8. water supply connectors, 1-9. insulated chassis, 2. fastening bolts, 3. wires, 4. electrostatic occur
Device, 4-1. negative pole interfaces, 4-2. anode interfaces, 5. penstocks, 6. pressure pumps, 7. communicating pipes, 8. filters, 9. supply water
Pipe, 10. check-valves, 11. threeways, 12. frames, 13. pressure pure water, 14. pressurized tanks, 14-1. breathing interfaces, 14-2. auxiliary
Interface, 14-3. maintenance evacuated tubes, 15. compressed airs, 16. pressure controllers, 17. maintenance exhaust-valves, 18. pressure-bearing hydroeciums, 19.
Sealing gasket, 20. normally closed air bleeding valves.
Embodiment
In embodiment shown in the Fig. 1 of embodiment 1, a kind of aqueous medium gasified combustion apparatus is mainly by pressure pump 6, pressure
Power tank 14, burner assembly 1 and electrostatic generator 4 form, wherein, burner assembly 1 includes catalysis electrode 1-4, electrode takes up
Disk 1-1, duct cover disk 1-2 and insulated chassis 1-9, catalysis electrode 1-4 are 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, and catalysis electrode 1-4 upper semisection is in micropore conical structure, under catalysis electrode 1-4
It is more than one to have water guide duct 1-401, catalysis electrode 1-4 in half segment body；Electrode, which is taken up on disk 1-1, catalysis electrode 1-4's
Mounting hole；It is the up-small and down-big loudspeaker that falls to have the duct 1-3 of quantity identical with catalysis electrode 1-4, duct 1-3 on the cover disk 1-2 of duct
Shape structure；It is fluted in insulated chassis 1-9；Catalysis electrode 1-4 and duct cover disk 1-2 are taken up on disk 1-1 installed in electrode, are urged
The micropore cone of polarizing electrode 1-4 upper semisections is placed among duct cover disk 1-2 duct 1-3, catalysis electrode 1-4 and duct 1-3
Wall body between space form electrostatic field；Electrode takes up disk 1-1 on insulated chassis 1-9 and is enclosed in groove port,
Being taken up in electrode has metal backing 1-5 on the inside of disk 1-1, metal backing 1-5 is connected to catalysis electrode 1-4, in metal backing 1-5
On have conductive plug 1-6, have electrically conductive socket 1-7 on insulated chassis 1-9, the conductive plug 1-6 on metal backing 1-5 is inserted into
In electrically conductive socket 1-7 on insulated chassis 1-9, space forms pressure-bearing hydroecium 18, catalysis electrode 1- in insulated chassis 1-9 groove
4 water guide duct 1-401 is communicated to pressure-bearing hydroecium 18, and pressure-bearing hydroecium 18 has water supply connector 1-8 accesses；Electrically conductive socket 1-7 passes through
Wire is connected on the anode interface 4-2 of electrostatic generator 4, and duct cover disk 1-2 is wired to the negative of electrostatic generator 4
On the interface 4-1 of pole；The water supply connector 1-8 of pressure-bearing hydroecium 18 is connected on the pipeline between check-valves 10 and pressurized tank 14.This reality
Apply in example, being taken up in electrode on disk 1-1 has normally closed air bleeding valve 20, and normally closed air bleeding valve 20 is communicated to pressure-bearing hydroecium 18, first to use
When, open normally closed air bleeding valve 20, the air in pressure-bearing hydroecium 18 is discharged with water inlet, and it is easy into water to make；The bottom of pressurized tank 14
There is breathing interface 14-1, pressure controller 16 and maintenance exhaust-valve 17 are arranged at the top or top of pressurized tank 14, and pressure pump 6 goes out
The mouth of a river is attached by check-valves 10 and the breathing interface 14-1 of the bottom of pressurized tank 14；On the pipeline that pressure pump 6 accesses
There is filter 8.In the present embodiment, electrode takes up disk 1-1 and insulated chassis 1-9 and selects alumina ceramic material or zirconia ceramics
Material is made, and duct cover disk 1-2 is made from stainless steel material.
The present embodiment is used in Industrial Boiler, and burner assembly 1 is arranged in the burner hearth of Industrial Boiler, to duct cover disk
1-2 carries out ground protection processing, and pressure pump 6, pressurized tank 14 and electrostatic generator 4 are arranged on the periphery of Industrial Boiler.Work
When, to more than 10,000 volts of electrostatic of catalysis electrode 1-4 and duct cover disk 1-2 applications, justify catalysis electrode 1-4 upper semisection micropore
Cone is in the electrostatic field among the 1-3 of duct, to increase catalysis electrode 1-4 catalytic activity, and forms electricity to hydrone
From effect；Entered using pure water as raw water, the pressurized water pump 6 of raw water in the pressure-bearing hydroecium 18 of burner assembly 1,
Raw water is entered in pressurized tank by the bottom of pressurized tank 14 simultaneously, is compressed the upper air in pressurized tank 14, forms pressure
Contracting air, the water of the bottom of pressurized tank 14 have pressure in the presence of compressed air, hydraulic pressure and pressurized tank in pressure-bearing hydroecium 18
The hydraulic pressure of 14 bottoms is equal.The pure water with pressure penetrates into catalysis electrode by water guide duct 1-401 in pressure-bearing hydroecium 18
In 1-4 micro-pore, catalysis electrode 1-4 micro-pore filters to hydrone, macromolecular mass is turned into small molecule, water
The activity of molecule is improved, and makes hydrone be easier to be decomposed, meanwhile, catalysis electrode 1-4 nickel-sulfur alloy material is to water
Molecule is catalytically decomposed.Hydrone is changed into small molecular cluster structure, then close through nickel sulphur by pressure permeation by macromolecular mass
Golden material catalysis and electrostatic field ionization, are decomposed into hydrogen, oxygen and active hydrogen atom, active oxygen atom, reactive hydrogen oxygen atom
The activity chemistry thing of group, escapes from catalysis electrode 1-4 upper semisection micropore cone, turns into vaporising fuel, enter duct
In 1-3, the vaporising fuel of hydrone conversion is lighted by the high-voltage spark between catalysis electrode 1-4 and duct 1-3 wall bodies,
Back reaction burning is carried out, releases heat energy.In said process, the water of water and infiltration catalysis electrode 1-4 in pressure-bearing hydroecium 18 is to urging
Polarizing electrode 1-4 produces cooling effect, protects catalysis electrode 1-4 not to be burned.Operating pressure in pressurized tank 14 is by Stress control
Device 16 is controlled, and when threshold pression of the pressure in pressurized tank 14 less than setting, pressure controller 16 connects pressure pump 6
Power supply, pressure pump 6 is run, carry out moisturizing to pressurized tank 14, the air in pressurized tank 14 is compressed and is made pressure inside the tank liter
It is high；When the pressure in pressurized tank 14 reaches the pressure upper limit of setting, pressure controller 16 disconnects the power supply of pressure pump 6, makes
Pressure pump 6 stops, and by the control of pressure controller 16, makes the pressure in pressurized tank 14 constant in setting range.
Claims (7)
1. a kind of aqueous medium gasified combustion apparatus, including pressure pump, pressurized tank, burner and electrostatic generator, pressure pump
Delivery port be attached by the bottom of check-valves and pressurized tank, it is characterized in that burner assembly（1）By catalysis electrode（1-
4）, electrode take up disk（1-1）, duct cover disk（1-2）And insulated chassis（1-9）Composition, wherein, catalysis electrode（1-4）Form water
Molecular filtration and catalysis element, catalysis electrode（1-4）Upper semisection be in micropore conical structure, catalysis electrode（1-4）Lower half
There is water guide duct in segment body（1-401）, catalysis electrode（1-4）For more than one；Electrode takes up disk（1-1）On have catalysis electrode
（1-4）Mounting hole；Duct cover disk（1-2）On have and catalysis electrode（1-4）The duct of identical quantity（1-3）；Insulated chassis（1-
9）In it is fluted；Catalysis electrode（1-4）With duct cover disk（1-2）Disk is taken up installed in electrode（1-1）On, catalysis electrode（1-4）
The micropore cone of upper semisection is placed in duct cover disk（1-2）Duct（1-3）Among, catalysis electrode（1-4）With duct（1-3）'s
Space between wall body forms electrostatic field；Electrode takes up disk（1-1）Installed in insulated chassis（1-9）Go up and be enclosed in groove port
On, insulated chassis（1-9）Groove in space form pressure-bearing hydroecium（18）, catalysis electrode（1-4）Water guide duct（1-401）Even
Lead to pressure-bearing hydroecium（18）, pressure-bearing hydroecium（18）There is water supply connector（1-8）Access；The anode interface and negative pole of electrostatic generator connect
Mouth respectively with catalysis electrode（1-4）, duct cover disk（1-2）It is electrically connected, pressure-bearing hydroecium（18）Water supply connector（1-8）Even
It is connected to check-valves（10）With pressurized tank（14）Between pipeline on.
A kind of 2. aqueous medium gasified combustion apparatus according to claim 1, it is characterized in that catalysis electrode（1-4）For metal powder
The miillpore filter structure of end sintering, the micropore between metal dust form the filtration channel of hydrone.
A kind of 3. aqueous medium gasified combustion apparatus according to claim 1, it is characterized in that taking up disk in electrode（1-1）It is interior
There is metal backing side（1-5）, metal backing（1-5）It is connected to catalysis electrode（1-4）, in metal backing（1-5）On have conductive insert
Head（1-6）, in insulated chassis（1-9）On have electrically conductive socket（1-7）, during assembling, metal backing（1-5）On conductive plug（1-
6）It is inserted into insulated chassis（1-9）On electrically conductive socket（1-7）In, electrically conductive socket（1-7）It is wired to electrostatic
Device（4）Anode interface（4-2）On.
A kind of 4. aqueous medium gasified combustion apparatus according to claim 1, it is characterized in that taking up disk in electrode（1-1）On have
Normally closed air bleeding valve（20）, normally closed air bleeding valve（20）It is communicated to pressure-bearing hydroecium（18）.
A kind of 5. aqueous medium gasified combustion apparatus according to claim 1, it is characterized in that duct cover disk（1-2）On duct
（1-3）For up-small and down-big inverted tubaeform structure.
A kind of 6. aqueous medium gasified combustion apparatus according to claim 1, it is characterized in that the bottom of pressurized tank has breathing to connect
Mouthful（14-1）, the delivery port of pressure pump passes through check-valves（10）With the breathing interface of pressure pot bottom（14-1）It is attached.
A kind of 7. aqueous medium gasified combustion apparatus according to claim 1, it is characterized in that in pressure pump（6）The pipe of access
There is filter on road（8）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610662402.7A CN106145032B (en) | 2016-08-15 | 2016-08-15 | Aqueous medium gasified combustion apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610662402.7A CN106145032B (en) | 2016-08-15 | 2016-08-15 | Aqueous medium gasified combustion apparatus |
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| CN106145032A CN106145032A (en) | 2016-11-23 |
| CN106145032B true CN106145032B (en) | 2018-02-02 |
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| WO2006116849A1 (en) * | 2005-05-02 | 2006-11-09 | Cropley Holdings Ltd. | Method and apparatus for cooking using a combustible gas produced with an electrolyzer |
| WO2009009496A1 (en) * | 2007-07-06 | 2009-01-15 | Evaco, Llc. | Carbon free dissociation of water and production of hydrogen related power |
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| CN203402921U (en) * | 2013-07-11 | 2014-01-22 | 佳昊新能源投资有限公司 | Plasma-arc gas production equipment |
| CN205855992U (en) * | 2016-08-15 | 2017-01-04 | 衢州昀睿工业设计有限公司 | Aqueous medium gasified combustion apparatus |
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2016
- 2016-08-15 CN CN201610662402.7A patent/CN106145032B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2006116849A1 (en) * | 2005-05-02 | 2006-11-09 | Cropley Holdings Ltd. | Method and apparatus for cooking using a combustible gas produced with an electrolyzer |
| CN1824603A (en) * | 2006-01-13 | 2006-08-30 | 樊后鹏 | Hydrogen energy generator |
| WO2009009496A1 (en) * | 2007-07-06 | 2009-01-15 | Evaco, Llc. | Carbon free dissociation of water and production of hydrogen related power |
| CN101975407A (en) * | 2010-07-21 | 2011-02-16 | 袁宏文 | Water boiling furnace |
| CN203402921U (en) * | 2013-07-11 | 2014-01-22 | 佳昊新能源投资有限公司 | Plasma-arc gas production equipment |
| CN205855992U (en) * | 2016-08-15 | 2017-01-04 | 衢州昀睿工业设计有限公司 | Aqueous medium gasified combustion apparatus |
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| Publication number | Publication date |
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| CN106145032A (en) | 2016-11-23 |
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