CN106152472B - Water heater for converting water medium into fuel - Google Patents
Water heater for converting water medium into fuel Download PDFInfo
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- CN106152472B CN106152472B CN201610662401.2A CN201610662401A CN106152472B CN 106152472 B CN106152472 B CN 106152472B CN 201610662401 A CN201610662401 A CN 201610662401A CN 106152472 B CN106152472 B CN 106152472B
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- interface
- cover plate
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- 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
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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
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- 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
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- 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
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- 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
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- 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
The utility model provides a water heater of aqueous medium conversion fuel, relate to combustor and water heater equipment, including the combustor, the heat collector, electrostatic generator and casing, the combustor, heat collector and electrostatic generator install in the casing, the combustor subassembly comprises catalytic electrode, tubular electrode holder and cover plate, many catalytic electrodes are installed on tubular electrode holder, the cover plate passes through insulating support piece and installs on the body of tubular electrode holder, the micropore cone of catalytic electrode is arranged in the pore of cover plate, tubular electrode holder passes through insulating support and installs on the wall body of casing, the heat collector sets up the top at the combustor subassembly, the space between the heat collecting fin constitutes the thermal convection way, catalytic electrode carries out electric connection with electrostatic generator's positive interface, the cover plate carries out electric connection with electrostatic generator's negative pole interface. The invention decomposes water molecules into gasified fuel of oxyhydrogen for combustion, and uses water as an energy source to realize clean combustion and protect the ecological environment.
Description
Technical Field
The invention relates to a burner and water heater equipment, in particular to aqueous medium combustion equipment.
Background
The water is a substance containing the most abundant hydrogen elements, each water molecule is formed by combining two hydrogen atoms and one oxygen atom, more than 111 kilograms of hydrogen are contained in each cubic meter of water, the mass capacity of the water is more than 11.1 percent, the calorific value of the hydrogen is high, and the heat of 142120kj can be released by combusting 1 kilogram of hydrogen and is three times that of gasoline. Water is developed into an energy source to be applied, carbon dioxide is not generated during combustion, only water is generated as a product, and the product can be recycled, so that the method has great benefits for improving the acid rain environment of the atmosphere and reducing the content of carbon dioxide in the atmosphere, thereby lightening the greenhouse effect. Therefore, the development of the aqueous medium fuel not only can solve the situation of energy shortage, but also has outstanding environmental protection effect. However, hydrogen atoms and oxygen atoms in water molecules are bonded very firmly, the high-temperature heating method needs to heat the water molecules to more than 3000 ℃ for decomposition, and the general heating mode is difficult to reach the high temperature; the hydrogen is produced by decomposing water molecules by a current method in industry, the decomposition speed is slow, the efficiency is low, and the energy consumption is large.
Disclosure of Invention
The invention aims to overcome the defects of hydrogen production by water pyrolysis and hydrogen production by decomposing water molecules by an electric current method, and provides a water heater using water medium to convert fuel, which uses water as an energy source to realize clean combustion and protect the ecological environment.
The invention relates to a water heater for converting water media into fuel, which comprises a burner, a heat collector, an electrostatic generator and a casing, wherein the burner, the heat collector and the electrostatic generator are arranged in the casing, the top of the casing is provided with an exhaust interface, and the bottom of the casing is provided with a working water interface, and the water heater is characterized in that a burner component 5 consists of more than one catalytic electrode 5-4, a tubular electrode seat 5-8 and a cover plate 5-1, the upper half section of the catalytic electrode 5-4 is of a microporous cone structure, and the lower half section of the catalytic electrode 5-4 is provided with a water guide pore passage 5-401; the tubular electrode holder 5-8 is a hollow round tube structure with a closed tail end, and a row of screw ports 5-3 for mounting catalytic electrodes are arranged on the tubular electrode holder 5-8; the cover plate 5-1 is provided with pore channels 5-2 with the same number as the catalytic electrodes, and the pore channels 5-2 are in an inverted horn-shaped structure with a small upper part and a large lower part; a plurality of catalytic electrodes 5-4 are arranged on screw ports 5-3 of tubular electrode holders 5-8, water guide pore channels 5-401 in the catalytic electrodes 5-4 are communicated with the tube spaces of the tubular electrode holders 5-8, water inlet interfaces 5-10 are arranged at the front ends of the tubular electrode holders 5-8, and the tube spaces of the tubular electrode holders 5-8 form pressure bearing water chambers 5-9; the cover plate 5-1 is arranged on a tube body of the tubular electrode seat 5-8 through an insulating support piece 5-6, the microporous cone of the upper half section of the catalytic electrode 5-4 is arranged in a pore passage 5-2 of the cover plate 5-1, the tubular electrode seat 5-8 is arranged on the wall body of the machine shell through an insulating support 11, and a water inlet interface 5-10 of the tubular electrode seat 5-8 is connected with a working water interface at the bottom of the machine shell; the heat collector 4 is arranged above the burner component 5, the heat collector 4 consists of a heat collecting coil 4-1 and heat collecting fins 4-2, the heat collecting coil 4-1 is provided with a cold water input interface and a hot water output interface, and spaces among the heat collecting fins 4-2 form a heat convection channel; the catalytic electrode 5-4 is electrically connected with the positive interface of the electrostatic generator, and the cover plate 5-1 is electrically connected with the negative interface of the electrostatic generator.
In the invention, the catalytic electrode 5-4 is a microporous filter membrane structure sintered by metal powder, the catalytic electrode 5-4 forms a water molecule filtering and catalyzing element, the catalytic electrode 5-4 is a tungsten-nickel pseudo alloy part sintered by a material mixed with tungsten powder and nickel-sulfur alloy powder, tungsten and nickel-sulfur alloy are not mutually dissolved and intermetallic compounds are not formed during firing, the formed pseudo alloy structure is a two-phase structure of tungsten particles and nickel-sulfur alloy particles, micro pores exist in the pseudo alloy structure, the micro pores form a filtering channel of water molecules and have the effect of filtering the water molecules, and the nickel-sulfur alloy has a catalytic effect on the decomposition of the water molecules so that the water molecules are more easily decomposed; a space is arranged between the catalytic electrode 5-4 and the wall body of the pore channel 5-2 of the cover plate 5-1, and the space between the catalytic electrode 5-4 and the wall body of the pore channel 5-2 forms an electrostatic field; the tail end of the tubular electrode seat 5-8 is provided with a normally closed exhaust valve 5-7, and the normally closed exhaust valve 5-7 is communicated with the inner space of the tubular electrode seat 5-8; the water heater is provided with an external hot water tank 27, a cold water input interface 13 of the heat collecting coil 4-1 is connected with a circulating water outlet 27-3 of the external hot water tank 27, and a hot water output interface 3 of the heat collecting coil 4-1 is connected with a circulating water inlet 27-4 of the external hot water tank 27; the periphery of the water heater is provided with a pressure tank 23, a pressure water pump 18 and a check valve 19, the bottom of the pressure tank 23 is provided with a breathing interface 23-1, the water outlet of the pressure water pump 18 is connected to the breathing interface 23-1 at the bottom of the pressure tank 23 through the check valve 19, and the working water interface of the water heater is connected to a connecting pipeline between the check valve 19 and the breathing interface 23-1 at the bottom of the pressure tank 23.
When the water heater is applied, the front surface of the shell is provided with an operation panel, the operation panel is provided with a power switch button and a hot water temperature setting button, and the operation instruction controls the operation or stop of the pressurizing water pump 18 and the electrostatic generator 8 through the microprocessor. When the device works, more than 1 ten thousand volts of static electricity is applied between the catalytic electrode 5-4 and the cover plate 5-1, so that the micropore cone at the upper half section of the catalytic electrode 5-4 is positioned in the electrostatic field in the pore channel 5-2, the catalytic activity of the catalytic electrode 5-4 is increased, and an ionization effect is formed on water molecules; pure water is used as raw material water, the raw material water enters a pressure bearing chamber 5-9 of a burner assembly 5 through a pressure water pump 18, meanwhile, the raw material water enters a pressure tank from a breathing port 23-1 at the bottom of the pressure tank 23, so that air at the upper part in the pressure tank 23 is compressed to form compressed air, water at the lower part of the pressure tank 23 has pressure under the action of the compressed air, and the water pressure in the pressure bearing chamber 5-9 is equal to the water pressure at the lower part of the pressure tank 23. The purified water with pressure in the pressure bearing water chamber 5-9 permeates into the tiny pores of the catalytic electrode 5-4 through the water guide pore canal 5-401, the tiny pores of the catalytic electrode 5-4 filter water molecules, so that large molecular groups become small molecules, the activity of the water molecules is improved, the water molecules are more easily decomposed, and meanwhile, the nickel-sulfur alloy material of the catalytic electrode 5-4 carries out catalytic decomposition on the water molecules. Water molecules are permeated under pressure, converted into a small molecular group structure from a large molecular group, catalyzed by a nickel-sulfur alloy material and ionized by an electrostatic field, and decomposed into hydrogen, oxygen and active chemical substances of active hydrogen atoms, active oxygen atoms and active hydrogen-oxygen radicals, and then escaped from a micropore cone at the upper half section of a catalytic electrode 5-4 to form gasified fuel, the gasified fuel enters a pore canal 5-2, the gasified fuel converted from the water molecules is ignited by high-pressure electric sparks between the catalytic electrode 5-4 and the wall body of the pore canal 5-2 to perform reverse reaction combustion, heat energy is released to heat water in a heat collecting coil 4-1, the water in the heat collecting coil 4-1 is heated and then is output by a hot water output interface 3, the water enters an external hot water tank through a circulating water inlet of the external hot water tank, and cold water in the external hot water tank enters a heat collecting coil 4 through a circulating water outlet and a cold water input interface 13 of the heat collecting coil 4-1 to the heat collecting coil 4 1, performing cyclic heating, and repeating the steps until the hot water in the external hot water tank reaches the set temperature, stopping the water heater, and when the hot water in the external hot water tank is lower than the set temperature, restoring the water heater to work. In the process, the water in the pressure bearing water chamber 5-9 and the water permeating into the catalytic electrode 5-4 cool the catalytic electrode 5-4, so that the catalytic electrode 5-4 is protected from being burnt out. The invention adopts static electricity to improve the catalytic activity of the catalytic electrode 5-4 and utilizes the electrostatic field to ionize water molecules, converts water media into fuels for utilization, reduces the temperature requirement of water pyrolysis molecules, consumes little electric energy and has high decomposition efficiency of the water molecules.
The invention has the beneficial effects that: a water heater for providing water medium to convert fuel features that the water medium is used as gasifying raw material, the water molecules are pressure permeated to transform the large molecular groups into small molecular groups, and the gasified fuel is decomposed into hydrogen and oxygen by the catalysis of Ni-S alloy and the ionization of electrostatic field.
Drawings
FIG. 1 is a block diagram of an aqueous medium reforming fuel water heater according to the present invention.
Fig. 2 is a detailed view of the burner assembly of the present invention.
Fig. 3 is an enlarged view of the catalytic electrode of the present invention.
FIG. 4 is a water heater peripheral of the present invention.
In the figure: 1. an exhaust port, 2 a machine shell, 3 a hot water output port, 4 a heat collector, 4-1 a heat collecting coil pipe, 4-2 heat collecting fins, 5 a burner component, 5-1 a cover plate, 5-2 pore channels, 5-3 screw ports, 5-4 catalytic electrodes, 5-401 water guide pore channels, 5-402 external threads, 5-403 external hexagon bodies, 5-404 microporous cones, 5-5 positioning screws, 5-6 insulating support pieces, 5-7 normally closed exhaust valves, 5-8 tubular electrode seats, 5-9 pressure bearing water chambers, 5-10 water inlet ports, 6 high voltage wires, 7 return lines, 8 electrostatic generators, 8-1 positive ports, 8-2 negative ports and 8-3 power wires, 9. the device comprises a working water interface, a connecting pipe, 11, an insulating support, 12, a water inlet joint, 13, a cold water input interface, 14, a working water pipe, 15, a water supply pipe, 16, a filter, 17, a communicating pipe, 18, a pressure water pump, 19, a check valve, 20, a tee joint, 21, a frame, 22, pressure purified water, 23, a pressure tank, 23-1, a breathing interface, 23-2, an auxiliary interface, 23-3, a maintenance emptying pipe, 24, compressed air, 25, a pressure controller, 26, a maintenance emptying valve, 27, a hot water tank, 27-1, a user hot water outlet, 27-2, a tap water supplement interface, 27-3, a circulating water outlet, 27-4, a circulating water inlet, 28, an automatic exhaust valve, 29, an insulating layer and 30 hot water.
Detailed Description
Example 1 in the embodiment shown in fig. 1-4, a water heater for converting water media into fuel mainly comprises a burner assembly 5, a heat collector 4, an electrostatic generator 8 and a casing 2, wherein the burner assembly 5, the heat collector 4 and the electrostatic generator 8 are installed in the casing 2, an exhaust port 1 is arranged at the top of the casing 2, a working water port 9 is arranged at the bottom of the casing 2, the burner assembly 5 comprises more than one catalytic electrode 5-4, a tubular electrode holder 5-8 and a cover plate 5-1, wherein the upper half section of the catalytic electrode 5-4 is in a microporous cone structure, and the lower half section of the catalytic electrode 5-4 is provided with a water guide pore passage 5-401; the tubular electrode holder 5-8 is a hollow round tube structure with a closed tail end, and a row of screw ports 5-3 for mounting catalytic electrodes are arranged on the tubular electrode holder 5-8; the cover plate 5-1 is provided with pore channels 5-2 with the same number as the catalytic electrodes, and the pore channels 5-2 are in an inverted horn-shaped structure with a small upper part and a large lower part; a plurality of catalytic electrodes 5-4 are arranged on screw ports 5-3 of tubular electrode holders 5-8, water guide pore passages 5-401 in the catalytic electrodes 5-4 are communicated with the tube space of the tubular electrode holders 5-8, the front ends of the tubular electrode holders 5-8 are provided with water inlet ports 5-10, the tube space of the tubular electrode holders 5-8 forms a pressure bearing water chamber 5-9, the tail ends of the tubular electrode holders 5-8 are provided with normally closed exhaust valves 5-7, and the normally closed exhaust valves 5-7 are communicated with the tube space of the tubular electrode holders 5-8; the cover plate 5-1 is arranged on a tube body of the tubular electrode seat 5-8 through an insulating support member 5-6, a micropore cone at the upper half section of the catalytic electrode 5-4 is arranged in a pore passage 5-2 of the cover plate 5-1, a space is arranged between the catalytic electrode 5-4 and a wall body of the pore passage 5-2 of the cover plate 5-1, the tubular electrode seat 5-8 is arranged on a wall body of a machine shell through an insulating support 11, and a water inlet interface 5-10 of the tubular electrode seat 5-8 is connected with a working water interface at the bottom of the machine shell; the heat collector 4 is arranged above the burner component 5, the heat collector 4 consists of a heat collecting coil 4-1 and heat collecting fins 4-2, the heat collecting coil 4-1 is provided with a cold water input interface and a hot water output interface, and spaces among the heat collecting fins 4-2 form a heat convection channel; the catalytic electrode 5-4 is electrically connected with the positive interface of the electrostatic generator, the cover plate 5-1 is electrically connected with the negative interface of the electrostatic generator, and the space between the catalytic electrode 5-4 and the wall body of the pore canal 5-2 forms an electrostatic field. In the embodiment, the catalytic electrode 5-4 is a microporous filter membrane structure sintered by metal powder, the catalytic electrode 5-4 forms a water molecule filtering and catalytic element, the catalytic electrode 5-4 is a tungsten-nickel pseudo alloy part sintered by a material mixed by tungsten powder and nickel-sulfur alloy powder, tungsten and nickel-sulfur alloy are not mutually dissolved and do not form intermetallic compounds when being fired, the formed pseudo alloy structure is a two-phase structure of tungsten particles and nickel-sulfur alloy particles, micro pores exist in the pseudo alloy structure, the micro pores form a filtering channel of water molecules and have the effect of filtering the water molecules, and the nickel-sulfur alloy has a catalytic effect on the decomposition of the water molecules so that the water molecules are more easily decomposed; the water heater is provided with an external hot water tank 27, the top of the hot water tank 27 is provided with an automatic exhaust valve 28, the bottom of the hot water tank 27 is provided with a tap water supplement interface 27-2, the middle part of the left side of the hot water tank 27 is provided with a circulating water inlet 27-4 for access, the lower part of the left side of the hot water tank 27 is provided with a circulating water outlet 27-3 for access, the upper part of the right side of the hot water tank 27 is provided with a user hot water outlet 27-1 for access, a cold water input interface 13 of a heat collecting coil 4-1 is connected with the circulating water outlet 27-3 of the hot water tank 27, and a hot water output interface 3 of the heat collecting coil 4-1 is connected with the circulating water inlet 27-4 of the hot water tank 27; the periphery of the water heater is provided with a pressure tank 23, a pressure water pump 18 and a check valve 19, the bottom of the pressure tank 23 is provided with a breathing interface 23-1, the water outlet of the pressure water pump 18 is connected to the breathing interface 23-1 at the bottom of the pressure tank 23 through the check valve 19, and the working water interface of the water heater is connected to a connecting pipeline between the check valve 19 and the breathing interface 23-1 at the bottom of the pressure tank 23; a filter 16 is arranged on a pipeline connected with a pressure water pump 18; a pressure controller 25 and a service drain valve 26 are provided in the upper or top part of the pressure tank 23; when the water-saving water tank is used for the first time, the normally closed exhaust valve 5-7 is opened, and air in the pressure bearing water chamber 5-9 is exhausted along with water inflow, so that the water inflow is easy.
When the water heater is applied, the front surface of the shell is provided with an operation panel, and the operation panel is provided with a power switch button and a hot water temperature setting button. When the device works, more than 1 ten thousand volts of static electricity is applied between the catalytic electrode 5-4 and the cover plate 5-1, so that the micropore cone at the upper half section of the catalytic electrode 5-4 is positioned in the electrostatic field in the pore channel 5-2, the catalytic activity of the catalytic electrode 5-4 is increased, and an ionization effect is formed on water molecules; pure water is used as raw material water, the raw material water enters a pressure bearing chamber 5-9 of a burner assembly 5 through a pressure water pump 18, meanwhile, the raw material water enters a pressure tank from a breathing port 23-1 at the bottom of the pressure tank 23, so that air at the upper part in the pressure tank 23 is compressed to form compressed air, water at the lower part of the pressure tank 23 has pressure under the action of the compressed air, and the water pressure in the pressure bearing chamber 5-9 is equal to the water pressure at the lower part of the pressure tank 23. The purified water with pressure in the pressure bearing water chamber 5-9 permeates into the tiny pores of the catalytic electrode 5-4 through the water guide pore canal 5-401, the tiny pores of the catalytic electrode 5-4 filter water molecules, so that large molecular groups become small molecules, the activity of the water molecules is improved, the water molecules are more easily decomposed, and meanwhile, the nickel-sulfur alloy material of the catalytic electrode 5-4 carries out catalytic decomposition on the water molecules. Water molecules are permeated under pressure, converted into a small molecular group structure from a large molecular group, catalyzed by a nickel-sulfur alloy material and ionized by an electrostatic field, and decomposed into hydrogen, oxygen and active chemical substances of active hydrogen atoms, active oxygen atoms and active hydrogen-oxygen radicals, and then escaped from a micropore cone at the upper half section of a catalytic electrode 5-4 to form gasified fuel, the gasified fuel enters a pore canal 5-2, the gasified fuel converted from the water molecules is ignited by high-pressure electric sparks between the catalytic electrode 5-4 and the wall body of the pore canal 5-2 to perform reverse reaction combustion, heat energy is released to heat water in a heat collecting coil 4-1, the water in the heat collecting coil 4-1 is heated and then is output by a hot water output interface 3, the water enters an external hot water tank through a circulating water inlet of the external hot water tank, and cold water in the external hot water tank enters a heat collecting coil 4 through a circulating water outlet and a cold water input interface 13 of the heat collecting coil 4-1 to the heat collecting coil 4 1, performing cyclic heating, and repeating the steps until the hot water in the external hot water tank reaches the set temperature, stopping the water heater, and when the hot water in the external hot water tank is lower than the set temperature, restoring the water heater to work. In the working process, the operating pressure in the pressure tank 23 is sampled by the pressure controller 25 and is controlled by the microprocessor, when the pressure in the pressure tank 23 is lower than the set lower limit pressure, the microprocessor is connected with the power supply of the pressure water pump 18 through an actuating element to enable the pressure water pump 18 to operate, water is supplemented to the pressure tank 23, and the air in the pressure tank 23 is compressed to enable the pressure in the pressure tank to rise; when the pressure in the pressure tank 23 reaches the set upper limit pressure, the microprocessor cuts off the power supply of the pressure water pump 18 through the actuator to stop the pressure water pump 18, and the pressure in the pressure tank 23 is kept constant within the set range by sampling through the pressure controller 25 and controlling through the microprocessor.
Claims (6)
1. A water heater for converting water media into fuel comprises a burner, a heat collector, an electrostatic generator and a casing, wherein the burner, the heat collector and the electrostatic generator are arranged in the casing, an exhaust interface is arranged at the top of the casing and a working water interface is arranged at the bottom of the casing and is connected, and the water heater is characterized in that a burner component (5) consists of more than one catalytic electrode (5-4), a tubular electrode holder (5-8) and a cover plate (5-1), the upper half section of the catalytic electrode (5-4) is of a microporous cone structure, and a water guide pore channel (5-401) is arranged in the lower half section of the catalytic electrode (5-4); the tubular electrode holder (5-8) is of a hollow round tube structure with a closed tail end, and a row of screw ports (5-3) for mounting catalytic electrodes are arranged on the tubular electrode holder (5-8); the cover plate (5-1) is provided with pore channels (5-2) with the same number as the catalytic electrodes, and the pore channels (5-2) are in inverted horn-shaped structures with small upper parts and large lower parts; a plurality of catalytic electrodes (5-4) are arranged on screw ports (5-3) of tubular electrode holders (5-8), water guide pore passages (5-401) in the catalytic electrodes (5-4) are communicated with the tube spaces of the tubular electrode holders (5-8), water inlet interfaces (5-10) are arranged at the front ends of the tubular electrode holders (5-8), and the tube spaces of the tubular electrode holders (5-8) form pressure bearing water chambers (5-9); the cover plate (5-1) is arranged on a tube body of the tubular electrode seat (5-8) through an insulating support piece (5-6), the microporous cone of the upper half section of the catalytic electrode (5-4) is arranged in a pore channel (5-2) of the cover plate (5-1), the tubular electrode seat (5-8) is arranged on the wall body of the machine shell through an insulating support (11), and a water inlet interface (5-10) of the tubular electrode seat (5-8) is connected with a working water interface at the bottom of the machine shell; the heat collector (4) is arranged above the burner component (5), the heat collector (4) is composed of a heat collecting coil (4-1) and heat collecting fins (4-2), the heat collecting coil (4-1) is provided with a cold water input interface and a hot water output interface, and spaces among the heat collecting fins (4-2) form a heat convection channel; the catalytic electrode (5-4) is electrically connected with the positive interface of the electrostatic generator, and the cover plate (5-1) is electrically connected with the negative interface of the electrostatic generator.
2. The water heater for converting water medium into fuel as claimed in claim 1, wherein the catalytic electrode (5-4) is a metal powder sintered microporous filter membrane structure, and the catalytic electrode (5-4) constitutes a water molecule filtering and catalyzing element.
3. A water heater for converting an aqueous medium into a fuel as claimed in claim 1, wherein a space is provided between the catalytic electrode (5-4) and the wall of the duct (5-2) of the cover plate (5-1), and the space between the catalytic electrode (5-4) and the wall of the duct (5-2) forms an electrostatic field.
4. The water heater for converting the water medium into the fuel as claimed in claim 1, wherein the tail end of the tubular electrode holder (5-8) is provided with a normally closed exhaust valve (5-7), and the normally closed exhaust valve (5-7) is communicated with the inner space of the tubular electrode holder (5-8).
5. The water heater for converting the water medium into the fuel as claimed in claim 1, wherein the water heater is provided with an external hot water tank (27), the cold water input interface (13) of the heat collecting coil (4-1) is connected with the circulating water outlet (27-3) of the external hot water tank (27), and the hot water output interface (3) of the heat collecting coil (4-1) is connected with the circulating water inlet (27-4) of the external hot water tank (27).
6. The water heater for converting the water medium into the fuel as claimed in claim 1, wherein a pressure tank (23), a pressure water pump (18) and a check valve (19) are arranged at the periphery of the water heater, a breathing port (23-1) is arranged at the bottom of the pressure tank (23), a water outlet of the pressure water pump (18) is connected to the breathing port (23-1) at the bottom of the pressure tank (23) through the check valve (19), and a working water port of the water heater is connected to a connecting pipeline between the check valve (19) and the breathing port (23-1) at the bottom of the pressure tank (23).
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 |
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| 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 |
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| CN106152472A CN106152472A (en) | 2016-11-23 |
| CN106152472B true CN106152472B (en) | 2021-10-26 |
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| CN111267705B (en) * | 2020-01-15 | 2021-08-24 | 湖南双达机电有限责任公司 | Heating device and installation method thereof |
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| CN2182366Y (en) * | 1993-11-24 | 1994-11-09 | 一○一六研究院 | Hydrogen-oxygen-combustion water heater |
| CN101525753B (en) * | 2008-03-04 | 2012-04-18 | 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 |
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