CN106152472A - Aqueous medium converts the water heater of fuel - Google Patents
Aqueous medium converts the water heater of fuel Download PDFInfo
- Publication number
- CN106152472A CN106152472A CN201610662401.2A CN201610662401A CN106152472A CN 106152472 A CN106152472 A CN 106152472A CN 201610662401 A CN201610662401 A CN 201610662401A CN 106152472 A CN106152472 A CN 106152472A
- Authority
- CN
- China
- Prior art keywords
- water
- interface
- catalysis electrode
- tubular pole
- pole seat
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H1/00—Water heaters, e.g. boilers, continuous-flow heaters or water-storage heaters
- F24H1/0027—Water heaters, e.g. boilers, continuous-flow heaters or water-storage heaters using fluid fuel
-
- 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
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H9/00—Details
- F24H9/0005—Details for water heaters
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H9/00—Details
- F24H9/18—Arrangement or mounting of grates or heating means
- F24H9/1809—Arrangement or mounting of grates or heating means for water heaters
- F24H9/1832—Arrangement or mounting of combustion heating means, e.g. grates or burners
- F24H9/1836—Arrangement or mounting of combustion heating means, e.g. grates or burners using fluid fuel
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H9/00—Details
- F24H9/20—Arrangement or mounting of control or safety devices
- F24H9/2007—Arrangement or mounting of control or safety devices for water heaters
- F24H9/2035—Arrangement or mounting of control or safety devices for water heaters using fluid 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
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Inorganic Chemistry (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
A kind of aqueous medium converts the water heater of fuel, relate to burner and water heater arrangement, including burner, heat collector, electrostatic generator and casing, burner, heat collector and electrostatic generator are arranged in casing, burner assembly is by catalysis electrode, tubular pole seat and cover plate composition, many catalysis electrodes are arranged on tubular pole seat, cover plate is arranged on the body of tubular pole seat by insulated support, the micropore cone of catalysis electrode is placed in the duct of cover plate, tubular pole seat is arranged on the wall body of casing by insulating support, heat collector is arranged on the top of burner assembly, space between thermal-arrest fin constitutes thermal convection current passage, catalysis electrode is electrically connected with the anode interface of electrostatic generator, cover plate is electrically connected with the negative pole interface of electrostatic generator.The present invention burns the vaporising fuel that water-molecule dissociation is hydrogen-oxygen, and water is applied as a kind of energy, it is achieved cleaning burning, preserves the ecological environment.
Description
Technical field
The present invention relates to burner and water heater arrangement, especially relate to a kind of aqueous medium combustion apparatus.
Background technology
Water is a kind of material the abundantest 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
Burn 1 kg hydrogen and can release the heat of 142120kj, be three times of gasoline.Water is developed into a kind of energy apply, during burning
Not producing carbon dioxide, product only has water, can be repeatedly circulated, and to improving air acid rain environment, reduces dioxy in air
Change carbon content, thus alleviate greenhouse effect and have great benefit.Therefore, exploitation aqueous medium fuel not only can solve energy shortage
Situation, and environment protecting highlight.But, hydrogen atom and oxygen atom in hydrone combine the most firm, high-temperature heating
Method need to be heated to 3000 DEG C of decomposition carried out above hydrone, and general mode of heating is difficult to reach the highest temperature；Industry
Upper current method decomposition water molecule hydrogen manufacturing, decomposition rate is slow, efficiency is low, and it is the biggest to consume energy.
Summary of the invention
The invention aims to overcome existing pyrolysis water hydrogen manufacturing and the shortcoming of current method decomposition water molecule hydrogen manufacturing, it is provided that one
Plant aqueous medium and convert the water heater of fuel, water is applied as a kind of energy, it is achieved cleaning burning, preserve the ecological environment.
A kind of aqueous medium of the present invention converts the water heater of fuel, including burner, heat collector, electrostatic generator and machine
Shell, burner, heat collector and electrostatic generator be arranged in casing, and the top of casing has exhaust port to pick out, the bottom of casing
There is working water interface to access, it is characterized in that burner assembly 5 is made up of catalysis electrode 5-4, tubular pole seat 5-8 and cover plate 5-1,
Wherein, catalysis electrode 5-4 is more than one, and the upper semisection of catalysis electrode 5-4 is micropore conical structure, catalysis electrode 5-4's
Lower half segment body has water guide duct 5-401；Tubular pole seat 5-8 is the hollow circular-tube structure of endcapped, at tubular pole seat
A row is had for installing the screw socket 5-3 of catalysis electrode on 5-8；The duct 5-2 with catalysis electrode equal number is had on cover plate 5-1,
Duct 5-2 is up-small and down-big inverted tubaeform structure；Many catalysis electrode 5-4 are arranged on the screw socket 5-3 of tubular pole seat 5-8
On, the water guide duct 5-401 in catalysis electrode 5-4 body connects with space in the pipe of tubular pole seat 5-8, at tubular pole seat 5-
The front end of 8 has into water interface 5-10, and in the pipe of tubular pole seat 5-8, space constitutes pressure-bearing hydroecium 5-9；Cover plate 5-1 is by insulation
Support member 5-6 is arranged on the body of tubular pole seat 5-8, and the micropore cone of catalysis electrode 5-4 upper semisection is placed in cover plate 5-1
Duct 5-2 among, tubular pole seat 5-8 is arranged on the wall body of casing by insulating support 11, and tubular pole seat 5-8 enters
Water interface 5-10 is attached with the working water interface of bottom of shell；Heat collector 4 is arranged on the top of burner assembly 5, thermal-arrest
Device 4 is made up of collection hot coil 4-1 and thermal-arrest fin 4-2, and collection hot coil 4-1 has cold water input interface to access and hot water output interface
Picking out, the space between thermal-arrest fin 4-2 constitutes thermal convection current passage；Catalysis electrode 5-4 enters with the anode interface of electrostatic generator
Row electrical connection, cover plate 5-1 is electrically connected with the negative pole interface of electrostatic generator.
In the present invention, catalysis electrode 5-4 is metal powder sintered microporous filter membrane structure, and catalysis electrode 5-4 constitutes moisture
Son filters and catalysis element, and catalysis electrode 5-4 is that the material of tungsten powder and the mixing of nickel-sulfur alloy powder sinters tungsten nickel pseudo-alloy into
Part, when firing, tungsten, nickel-sulfur alloy neither mutual phased soln, also it is formed without intermetallic compound, the pseudo-alloy formed is organized as
, there is micro-pore in tungsten particle, two phase structures of nickel-sulfur alloy granule, micro-pore constitutes the mistake of hydrone in pseudo-alloy tissue
Filter passage, has the effect filtering hydrone, and nickel-sulfur alloy therein has catalytic action to the decomposition of hydrone, makes hydrone
It is easier to decompose；Space, catalysis electrode 5-4 and duct 5-2 wall is had between the duct 5-2 wall body of catalysis electrode 5-4 and cover plate 5-1
Space between body constitutes electrostatic field；Tail end at tubular pole seat 5-8 has normally closed air bleeding valve 5-7, normally closed air bleeding valve 5-7 to connect
Space in the pipe of tubular pole seat 5-8；Water heater has external boiler 27, the cold water input interface 13 of collection hot coil 4-1
It is attached with the circulating outlet 27-3 of external hot water tank 27, the hot water output interface 3 of collection hot coil 4-1 and external hot water tank
The circulation water inlet 27-4 of 27 is attached；The outer of water heater is with pressurized tank 23, pressure pump 18 and check-valves 19, pressurized tank
Breathing interface 23-1 is arranged at the bottom of 23, and the outlet of pressure pump 18 is connected to the breathing bottom pressurized tank 23 by check-valves 19
Interface 23-1, the working water interface of water heater is connected to the company between the breathing interface 23-1 bottom check-valves 19 and pressurized tank 23
On adapter road.
The water heater of the present invention, in use, there is guidance panel in the front of casing, guidance panel has power switch button
Setting button with hot water temperature, operational order controls pressure pump 18 by microprocessor and electrostatic generator 8 runs or stops.
During work, to applying the electrostatic of more than 10,000 volts between catalysis electrode 5-4 and cover plate 5-1, make the micro-of catalysis electrode 5-4 upper semisection
Hole cone is in the electrostatic field among the 5-2 of duct, to increase the catalysis activity of catalysis electrode 5-4, and to hydrone shape
Become ionization；Using pure water as raw water, the pressurized water pump of raw water 18 enters into the pressure-bearing hydroecium of burner assembly 5
In 5-9, raw water is entered in pressurized tank by the breathing interface 23-1 bottom pressurized tank 23 simultaneously, makes the top in pressurized tank 23 empty
Gas is compressed, and forms compressed air, and the water of pressurized tank 23 bottom has pressure, pressure-bearing hydroecium 5-under compressed-air actuated effect
Hydraulic pressure in 9 is equal with the hydraulic pressure of pressurized tank 23 bottom.There is the pure water of pressure by water guide duct 5-in pressure-bearing hydroecium 5-9
In 401 micro-pores penetrating into catalysis electrode 5-4, hydrone is filtered by the micro-pore of catalysis electrode 5-4, makes big point
Son group becomes little molecule, and the activity of hydrone is improved, and makes hydrone be easier to be decomposed, meanwhile, and catalysis electrode 5-4's
Nickel-sulfur alloy material carries out catalytic decomposition to hydrone.Hydrone, through pressure permeation, is changed into little molecule by macromolecular mass
Unity structure, then ionize through the catalysis of nickel-sulfur alloy material and electrostatic field, it is decomposed into hydrogen, oxygen and active hydrogen atom, active oxygen
Atom, the activity chemistry thing of reactive hydrogen oxygen atomic group, escape from the micropore cone of catalysis electrode 5-4 upper semisection, become gas
Changing fuel, enter in the 5-2 of duct, the vaporising fuel that hydrone converts is by the height between catalysis electrode 5-4 and duct 5-2 wall body
Piezo spark is lighted, and carries out back reaction burning, releases heat energy, the water in collection hot coil 4-1 is heated, collects hot coil
Export by entering into hot water output interface 3 after water heating in 4-1, enter into external by the circulation water inlet of external hot water tank
In boiler, the cold water in external hot water tank is entered into by the cold water input interface 13 of circulating outlet and collection hot coil 4-1
It is circulated heating in collection hot coil 4-1, so goes round and begins again, until the hot water in external hot water tank reaches the temperature set,
Water heater quits work, and when the hot water in external hot water tank is less than the temperature set, water heater is resumed work.Said process
In, the water of the water in pressure-bearing hydroecium 5-9 and infiltration catalysis electrode 5-4 produces cooling effect, protection catalysis electricity to catalysis electrode 5-4
Pole 5-4 is not burned.The present invention uses electrostatic to improve the catalysis activity of catalysis electrode 5-4 and to utilize electrostatic field to ionize moisture
Son, is converted into fuel utilization aqueous medium, reduces the temperature requirement of pyrolysis hydrone, and institute's consuming electric power is few, dividing of hydrone
Solution efficiency is high.
The invention has the beneficial effects as follows: provide aqueous medium to convert the water heater of fuel, with aqueous medium as gasified raw material, water
Molecule passes through pressure permeation, macromolecular mass be changed into small molecular cluster structure, then through the catalysis of nickel-sulfur alloy material and electrostatic field electricity
From, the vaporising fuel being decomposed into hydrogen-oxygen burns, and water is applied as a kind of energy, it is achieved cleaning burning, protecting ecology
Environment.
Accompanying drawing explanation
Fig. 1 is the water heater structure figure of the aqueous medium conversion fuel of the present invention.
Fig. 2 is the burner assembly detail drawing of the present invention.
Fig. 3 is the catalysis electrode enlarged drawing of the present invention.
Fig. 4 is the water heater ancillary equipment of the present invention.
In figure: 1. exhaust port, 2. casing, 3. hot water output interface, 4. heat collector, 4-1. collection hot coil, 4-2. thermal-arrest
Fin, 5. burner assembly, 5-1. cover plate, 5-2. duct, 5-3. screw socket, 5-4. catalysis electrode, 5-401. water guide duct, 5-
402. external screw threads, 5-403. outer-hexagonal body, 5-404. micropore cone, 5-5. positions screw, 5-6. insulated support, and 5-7. is normal
Closing air bleeding valve, 5-8. tubular pole seat, 5-9. pressure-bearing hydroecium, 5-10. intakes interface, 6. high-voltage line, 7. return line, and 8. electrostatic is sent out
Raw device, 8-1. anode interface, 8-2. negative pole interface, 8-3. power line, 9. working water interface, 10. connecting tube, 11. insulating supports,
12. water supply connectors, 13. cold water input interfaces, 14. work water pipes, 15. feed pipes, 16. filters, 17. communicating pipes, 18. pressurizations
Water pump, 19. check-valves, 20. threeways, 21. frames, 22. pressure pure water, 23. pressurized tanks, 23-1. breathes interface, and 23-2. is auxiliary
Adjuvant grafting mouth, 23-3. overhauls evacuated tube, 24. compressed airs, 25. pressure controllers, 26. maintenance exhaust-valves, 27. boilers, 27-
1. user's hot water outlet, 27-2. tap water supplements interface, 27-3. circulating outlet, and 27-4. circulates water inlet, and 28. arrange automatically
Air valve, 29. heat-insulation layers, 30. hot water.
Detailed description of the invention
In embodiment shown in embodiment 1 Fig. 1-4, aqueous medium converts the water heater of fuel mainly by burner assembly
5, heat collector 4, electrostatic generator 8 and casing 2 form, and burner assembly 5, heat collector 4 and electrostatic generator 8 are arranged on casing 2
In, the top of casing 2 has exhaust port 1 to pick out, and the bottom of casing 2 has working water interface 9 to access, and burner assembly 5 includes urging
Polarizing electrode 5-4, tubular pole seat 5-8 and cover plate 5-1, wherein, catalysis electrode 5-4 is more than one, the upper half of catalysis electrode 5-4
Section is micropore conical structure, has water guide duct 5-401 in the lower half segment body of catalysis electrode 5-4；Tubular pole seat 5-8 is end
The hollow circular-tube structure closed, has a row for installing the screw socket 5-3 of catalysis electrode on tubular pole seat 5-8；On cover plate 5-1
Having the duct 5-2 with catalysis electrode equal number, duct 5-2 is up-small and down-big inverted tubaeform structure；Many catalysis electrode 5-4
It is arranged on the screw socket 5-3 of tubular pole seat 5-8, the water guide duct 5-401 in catalysis electrode 5-4 body and tubular pole seat 5-8
Pipe in space connection, have into water interface 5-10, space structure in the pipe of tubular pole seat 5-8 in the front end of tubular pole seat 5-8
Becoming pressure-bearing hydroecium 5-9, the tail end at tubular pole seat 5-8 has normally closed air bleeding valve 5-7, normally closed air bleeding valve 5-7 to be communicated to tubular type electricity
Space in the pipe of electrode seat 5-8；Cover plate 5-1 is arranged on the body of tubular pole seat 5-8 by insulated support 5-6, catalysis electricity
The micropore cone of pole 5-4 upper semisection is placed among the duct 5-2 of cover plate 5-1, the duct 5-2 of catalysis electrode 5-4 and cover plate 5-1
Having space between wall body, tubular pole seat 5-8 is arranged on the wall body of casing by insulating support 11, tubular pole seat 5-8's
Water inlet interface 5-10 is attached with the working water interface of bottom of shell；Heat collector 4 is arranged on the top of burner assembly 5, collection
Hot device 4 is made up of collection hot coil 4-1 and thermal-arrest fin 4-2, and collection hot coil 4-1 has cold water input interface to access and hot water output connects
Mouth picks out, and the space between thermal-arrest fin 4-2 constitutes thermal convection current passage；Catalysis electrode 5-4 and the anode interface of electrostatic generator
Being electrically connected, cover plate 5-1 is electrically connected with the negative pole interface of electrostatic generator, catalysis electrode 5-4 and duct 5-2 wall
Space between body constitutes electrostatic field.In the present embodiment, catalysis electrode 5-4 is metal powder sintered microporous filter membrane structure, urges
Polarizing electrode 5-4 constitutes hydrone and filters and catalysis element, and catalysis electrode 5-4 is tungsten powder and the material of nickel-sulfur alloy powder mixing
Sinter tungsten nickel pseudo-alloy part into, when firing, tungsten, nickel-sulfur alloy neither mutual phased soln, also it is formed without intermetallic compound, institute's shape
The pseudo-alloy become is organized as two phase structures of tungsten particle, nickel-sulfur alloy granule, there is micro-pore, micro hole in pseudo-alloy tissue
Gap constitutes the filtration channel of hydrone, has the effect filtering hydrone, and the decomposition of hydrone is had by nickel-sulfur alloy therein
Catalytic action, makes hydrone be easier to decompose；Water heater has external boiler 27, and automatic exhaust steam valve is arranged at the top of boiler 27
28, the bottom of boiler 27 has tap water to supplement interface 27-2, and the middle part on the left of boiler 27 has circulation water inlet 27-4 to access,
Bottom on the left of boiler 27 has circulating outlet 27-3 to pick out, and user hot water outlet 27-1 is arranged at the top on the right side of boiler 27
Picking out, the cold water input interface 13 of collection hot coil 4-1 is attached with the circulating outlet 27-3 of boiler 27, collects hot coil 4-
The hot water output interface 3 of 1 is attached with the circulation water inlet 27-4 of boiler 27；Water heater outer is with pressurized tank 23, adds
Water pump 18 and check-valves 19, breathing interface 23-1 is arranged at the bottom of pressurized tank 23, and the outlet of pressure pump 18 passes through check-valves
19 are connected to the breathing interface 23-1 bottom pressurized tank 23, and the working water interface of water heater is connected to check-valves 19 and pressurized tank 23
On connecting line between the breathing interface 23-1 of bottom；The pipeline that pressure pump 18 accesses there is filter 16；At pressure
Pressure controller 25 and maintenance exhaust-valve 26 are arranged at the top of tank 23 or top；When using for the first time, open normally closed air bleeding valve 5-7, hold
Air in pumping chamber 5-9 is discharged with water inlet, and it is easy to make into water.
The water heater of the present invention, in use, there is guidance panel in the front of casing, guidance panel has power switch button
Button is set with hot water temperature.During work, to applying the electrostatic of more than 10,000 volts between catalysis electrode 5-4 and cover plate 5-1, make to urge
The micropore cone of polarizing electrode 5-4 upper semisection is in the electrostatic field among the 5-2 of duct, to increase the catalysis of catalysis electrode 5-4
Activity, and hydrone is formed ionization；Using pure water as raw water, the pressurized water pump of raw water 18 enters into combustion
In the pressure-bearing hydroecium 5-9 of burner assembly 5, raw water is entered in pressurized tank by the breathing interface 23-1 bottom pressurized tank 23 simultaneously,
Making the upper air in pressurized tank 23 be compressed, form compressed air, the water of pressurized tank 23 bottom is in compressed-air actuated effect
Under there is pressure, the hydraulic pressure in pressure-bearing hydroecium 5-9 is equal with the hydraulic pressure of pressurized tank 23 bottom.In pressure-bearing hydroecium 5-9, there is pressure
Pure water penetrated in the micro-pore of catalysis electrode 5-4 by water guide duct 5-401, the micro-pore of catalysis electrode 5-4
Filtering hydrone, make macromolecular mass become little molecule, the activity of hydrone is improved, and makes hydrone be easier to obtain
Decomposing, meanwhile, the nickel-sulfur alloy material of catalysis electrode 5-4 carries out catalytic decomposition to hydrone.Hydrone through pressure permeation,
It is changed into small molecular cluster structure by macromolecular mass, then ionizes through the catalysis of nickel-sulfur alloy material and electrostatic field, be decomposed into hydrogen, oxygen
And the activity chemistry thing of active hydrogen atom, active oxygen atom, reactive hydrogen oxygen atomic group, micro-from catalysis electrode 5-4 upper semisection
Escaping in the cone of hole, become vaporising fuel, enter in the 5-2 of duct, the vaporising fuel that hydrone converts is by catalysis electrode 5-4
And the high-voltage spark between the 5-2 wall body of duct is lighted, carry out back reaction burning, release heat energy, in collection hot coil 4-1
Water heat, export, by external hot water tank by entering into hot water output interface 3 after the water heating in collection hot coil 4-1
Circulation water inlet enter in external hot water tank, the cold water in external hot water tank by circulating outlet and collection hot coil 4-1
Cold water input interface 13 enter into collection hot coil 4-1 in be circulated heating, so go round and begin again, until in external hot water tank
Hot water reach set temperature, water heater quits work, when the hot water in external hot water tank less than set temperature time, hot water
Device is resumed work.In above-mentioned work process, the operation pressure in pressurized tank 23 is sampled by pressure controller 26, passes through microprocessor
It is controlled, when the pressure in pressurized tank 23 is less than the threshold pression set, and microprocessor connects pressure (hydraulic) water by executive component
The power supply of pump 18, makes pressure pump 18 run, and carries out moisturizing to pressurized tank 23, in making the compression of the air in pressurized tank 23 make tank
Pressure raises；When the pressure in pressurized tank 23 reaches the pressure upper limit set, microprocessor disconnects pressurization by executive component
The power supply of water pump 18, is made pressure pump 18 stop, being sampled by pressure controller 26 and microprocessor is controlled, make pressurized tank
Pressure in 23 keeps constant in the range of setting.
Claims (6)
1. aqueous medium converts a water heater for fuel, including burner, heat collector, electrostatic generator and casing, burner, collection
Hot device and electrostatic generator are arranged in casing, and the top of casing has exhaust port to pick out, and working water interface is arranged at the bottom of casing
Access, it is characterized in that burner assembly (5) is made up of catalysis electrode (5-4), tubular pole seat (5-8) and cover plate (5-1), its
In, catalysis electrode (5-4) is more than one, and the upper semisection of catalysis electrode (5-4) is micropore conical structure, catalysis electrode (5-
4) lower half segment body has water guide duct (5-401)；Tubular pole seat (5-8) is the hollow circular-tube structure of endcapped, at pipe
A row is had for installing the screw socket (5-3) of catalysis electrode on formula electrode tip holder (5-8)；Have identical with catalysis electrode on cover plate (5-1)
The duct (5-2) of quantity, duct (5-2) is up-small and down-big inverted tubaeform structure；Many catalysis electrodes (5-4) are arranged on tubular type
On the screw socket (5-3) of electrode tip holder (5-8), the water guide duct (5-401) in catalysis electrode (5-4) body and tubular pole seat (5-8)
Pipe in space connection, have in the front end of tubular pole seat (5-8) into water interface (5-10), in the pipe of tubular pole seat (5-8)
Space constitutes pressure-bearing hydroecium (5-9)；Cover plate (5-1) is arranged on the body of tubular pole seat (5-8) by insulated support (5-6)
On, the micropore cone of catalysis electrode (5-4) upper semisection is placed among the duct (5-2) of cover plate (5-1), tubular pole seat (5-
8) it is arranged on the wall body of casing by insulating support (11), at the bottom of the water inlet interface (5-10) of tubular pole seat (5-8) and casing
The working water interface in portion is attached；Heat collector (4) is arranged on the top of burner assembly (5), and heat collector (4) is by collection hot coil
(4-1) constituting with thermal-arrest fin (4-2), collection hot coil (4-1) has cold water input interface to access and hot water output interface picks out, collection
Space between hot fin (4-2) constitutes thermal convection current passage；Catalysis electrode (5-4) carries out electricity with the anode interface of electrostatic generator
Gas connects, and cover plate (5-1) is electrically connected with the negative pole interface of electrostatic generator.
A kind of aqueous medium the most according to claim 1 converts the water heater of fuel, it is characterized in that catalysis electrode (5-4) is for gold
Belonging to powder sintered microporous filter membrane structure, catalysis electrode (5-4) constitutes hydrone and filters and catalysis element.
A kind of aqueous medium the most according to claim 1 converts the water heater of fuel, it is characterized in that catalysis electrode (5-4) and cover
Having space between duct (5-2) wall body of plate (5-1), the space between catalysis electrode (5-4) and duct (5-2) wall body constitutes quiet
Electric field.
A kind of aqueous medium the most according to claim 1 converts the water heater of fuel, it is characterized in that at tubular pole seat (5-8)
Tail end have normally closed air bleeding valve (5-7), normally closed air bleeding valve (5-7) to be communicated to space in the pipe of tubular pole seat (5-8).
A kind of aqueous medium the most according to claim 1 converts the water heater of fuel, it is characterized in that water heater has external heat
Water tank (27), the cold water input interface (13) of collection hot coil (4-1) enters with the circulating outlet (27-3) of external hot water tank (27)
Row connects, and the hot water output interface (3) of collection hot coil (4-1) is carried out even with the circulation water inlet (27-4) of external hot water tank (27)
Connect.
A kind of aqueous medium the most according to claim 1 converts the water heater of fuel, it is characterized in that the outer of water heater is with pressure
Power tank (23), pressure pump (18) and check-valves (19), breathing interface (23-1), pressure pump are arranged at the bottom of pressurized tank (23)
(18) outlet is connected to the breathing interface (23-1) of pressurized tank (23) bottom, the working water of water heater by check-valves (19)
Interface is connected on the connecting line between the breathing interface (23-1) of check-valves (19) and pressurized tank (23) bottom.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610662401.2A CN106152472B (en) | 2016-08-15 | 2016-08-15 | Water heater for converting water medium into fuel |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610662401.2A CN106152472B (en) | 2016-08-15 | 2016-08-15 | Water heater for converting water medium into fuel |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN106152472A true CN106152472A (en) | 2016-11-23 |
| CN106152472B CN106152472B (en) | 2021-10-26 |
Family
ID=57330174
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610662401.2A Active CN106152472B (en) | 2016-08-15 | 2016-08-15 | Water heater for converting water medium into fuel |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106152472B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111267705A (en) * | 2020-01-15 | 2020-06-12 | 湖南双达机电有限责任公司 | Heating device and installation method thereof |
Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2182366Y (en) * | 1993-11-24 | 1994-11-09 | 一○一六研究院 | Hydrogen-oxygen-combustion water heater |
| CN101525753A (en) * | 2008-03-04 | 2009-09-09 | 黄国峰 | Water fuel feeding system |
| CN202057023U (en) * | 2011-05-12 | 2011-11-30 | 刘树平 | Water heater for alcohol-based liquid fuel |
| CN103233830A (en) * | 2013-04-28 | 2013-08-07 | 上海沃能环保科技有限公司 | Oxy-hydrogen hybrid power device |
| JP5674243B2 (en) * | 2011-02-24 | 2015-02-25 | 株式会社ノーリツ | Water heater |
| CN104378903A (en) * | 2014-11-11 | 2015-02-25 | 周开根 | Cathode of microporous membrane structure and plasma pyrolysis water spraying gun |
| CN204281299U (en) * | 2014-11-07 | 2015-04-22 | 广东合即得能源科技有限公司 | A kind of heating system based on Methanol water hydrogen production system |
| TWM516614U (en) * | 2015-03-27 | 2016-02-01 | Denwang Entpr Ltd | Fixing switch of telescopic rod and telescopic clothes rack structure improvement with the fixing switch |
| CN205860455U (en) * | 2016-08-15 | 2017-01-04 | 衢州昀睿工业设计有限公司 | Aqueous medium converts the water heater of fuel |
-
2016
- 2016-08-15 CN CN201610662401.2A patent/CN106152472B/en active Active
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2182366Y (en) * | 1993-11-24 | 1994-11-09 | 一○一六研究院 | Hydrogen-oxygen-combustion water heater |
| CN101525753A (en) * | 2008-03-04 | 2009-09-09 | 黄国峰 | Water fuel feeding system |
| JP5674243B2 (en) * | 2011-02-24 | 2015-02-25 | 株式会社ノーリツ | Water heater |
| CN202057023U (en) * | 2011-05-12 | 2011-11-30 | 刘树平 | Water heater for alcohol-based liquid fuel |
| CN103233830A (en) * | 2013-04-28 | 2013-08-07 | 上海沃能环保科技有限公司 | Oxy-hydrogen hybrid power device |
| CN204281299U (en) * | 2014-11-07 | 2015-04-22 | 广东合即得能源科技有限公司 | A kind of heating system based on Methanol water hydrogen production system |
| CN104378903A (en) * | 2014-11-11 | 2015-02-25 | 周开根 | Cathode of microporous membrane structure and plasma pyrolysis water spraying gun |
| TWM516614U (en) * | 2015-03-27 | 2016-02-01 | Denwang Entpr Ltd | Fixing switch of telescopic rod and telescopic clothes rack structure improvement with the fixing switch |
| CN205860455U (en) * | 2016-08-15 | 2017-01-04 | 衢州昀睿工业设计有限公司 | Aqueous medium converts the water heater of fuel |
Non-Patent Citations (2)
| Title |
|---|
| 张玉台: "《科技工程与经济社会协调发展 中国科协第五届青年学术年会文集》", 31 October 2004 * |
| 李伟: "《碱性水电解析氢活性阴极的研究》", 《中国优秀博硕士学位论文全文库(硕士)工程科技Ⅰ辑》 * |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111267705A (en) * | 2020-01-15 | 2020-06-12 | 湖南双达机电有限责任公司 | Heating device and installation method thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| CN106152472B (en) | 2021-10-26 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US7537623B2 (en) | Method and device for the producing of a gas rich in hydrogen by thermal pyrolysis of hydrocarbons | |
| CN104362355A (en) | Methanol water hydrogen-making machine and hydrogen-making method thereof | |
| CN105862062B (en) | A kind of system and method for electric waste heat hydrogen making and methanol more than Thermal generation unit | |
| CN209544526U (en) | A kind of hydrogen gas generating system of hydrogen current stabilization input | |
| CN206340608U (en) | A kind of methanol-water reformation hydrogen production generator | |
| CN104362359A (en) | Electric generator based on methanol water hydrogen-making system and electricity generation method thereof | |
| CN104276542A (en) | Reformer for hydrogen production system utilizing methyl alcohol and water, hydrogen production system utilizing methyl alcohol and water and hydrogen production method | |
| CN106784939B (en) | Methanol-water reforming hydrogen production generator | |
| CN204281299U (en) | A kind of heating system based on Methanol water hydrogen production system | |
| CN104445065A (en) | Heat supply system and heat supply method based on methanol water hydrogen production system | |
| CN106299410B (en) | A kind of solid oxide fuel cell power generating system using residual fuel self-heating | |
| CN205860455U (en) | Aqueous medium converts the water heater of fuel | |
| CN106152472A (en) | Aqueous medium converts the water heater of fuel | |
| CN104577164B (en) | Single turbine co-generation unit based on aluminum-water reaction and method | |
| CN205990231U (en) | The producing and burner of aqueous medium fuel | |
| CN205855992U (en) | Aqueous medium gasified combustion apparatus | |
| CN106698341B (en) | It is a kind of for starting the starter of methanol-water hydrogen production system employing reforming technology | |
| CN105826583B (en) | A kind of vehicle fuel battery co-generation unit and its working method | |
| CN205860013U (en) | A kind of aqueous medium gasification combustion system | |
| CN205990232U (en) | A kind of aqueous medium converts the burner of fuel | |
| CN106082124A (en) | A kind of aqueous medium converts the burner of fuel | |
| CN106082123B (en) | Aqueous medium fuel produce and burner | |
| CN106145032B (en) | Aqueous medium gasified combustion apparatus | |
| CN204185238U (en) | The reformer of Methanol water hydrogen production system and Methanol water hydrogen production system | |
| CN209339927U (en) | Overcritical underground coal gasification(UCG) output mixed gas trilogy supply electricity generation system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| TA01 | Transfer of patent application right | ||
| TA01 | Transfer of patent application right |
Effective date of registration: 20210929 Address after: 324000 No.19 huayuanqian, Quzhou City, Zhejiang Province Applicant after: QUZHOU YUXIN AGRICULTURAL PRODUCTS PROCESSING TECHNOLOGY DEVELOPMENT Co.,Ltd. Address before: 324000 B-302, room 2, 6 triumph South Road, Kecheng District, Quzhou, Zhejiang. Applicant before: QUZHOU YUNRUI INDUSTRIAL DESIGN Co.,Ltd. |
|
| GR01 | Patent grant | ||
| GR01 | Patent grant |