WO2010008237A2

WO2010008237A2 - Apparatus for gas extraction and thermal energy generation through high temperature degradation of h<sb>2</sb>o

Info

Publication number: WO2010008237A2
Application number: PCT/KR2009/003949
Authority: WO
Inventors: 나규성
Original assignee: Ra Kyu Sung
Priority date: 2008-07-17
Filing date: 2009-07-17
Publication date: 2010-01-21
Also published as: WO2010008237A3

Abstract

The present invention relates to an apparatus for gas extraction and thermal energy generation through high temperature degradation of H₂O; the apparatus according to the present invention is intended to obtain the useful resources hydrogen and oxygen by thermal degradation of water, and comprises a casing, a reactor tank that is installed inside said casing and that has a combustion furnace formed passing through its body, a heater part that is combined with said combustion furnace at one side to heat the reactor tank, a hydrogen extraction tube that is connected to one side of the top of said reactor tank to feed the hydrogen generated in the reactor tank into a hydrogen storage tank, a water supply tube that is connected to the side of said reactor tank to supply water, a temperature sensor that measures the temperature inside said reactor tank and transmits to a controller, and a controller that controls the operation of said heater part and valves depending upon the temperature inside said reactor tank.

Description

Gas extraction and heat energy generator according to high temperature decomposition of H₂O

The present invention relates to a gas extraction and thermal energy generating device according to the high temperature decomposition of H ₂ O, and more particularly to a technique for obtaining not only the energy by thermal decomposition of water, but also useful resources hydrogen and oxygen.

Various types of energy sources are used for driving power sources or cooling and heating.

The most widely used of these are underground buried coal and oil resources. These resources have been used for a long time and are widely used as energy sources for air conditioning, power generation, and transportation. However, these underground resources are difficult to collect and have a limited reserve. In addition, there is a problem that underground resources are polluted by the generation of harmful exhaust gases during combustion.

Nuclear resources are used as other energy sources. Nuclear resources use energy generated by the transformation of nuclear nuclei (nuclear fission and fusion), in particular nuclear power generation using fission. Although such nuclear resources have high energy generation efficiency and high utilization rates, there are problems in handling and waste disposal. In addition, since the miniaturization is difficult, there is a problem that the use is greatly limited.

To solve these problems, technologies using natural energy such as solar, wind and tidal power have been proposed. This natural energy has no problem of resource depletion, and there is an advantage that pollutants are not emitted due to power generation. However, power generation using natural energy is difficult to select a location for optimal power generation efficiency, high installation cost of equipment, and low efficiency.

The present invention was derived to solve the problems according to the prior art described above, and an object of the present invention is to provide a technique for obtaining hydrogen and oxygen, which are useful resources using water, which is easy to handle and obtain.

Another object of the present invention is to provide a technique capable of generating energy using extracted hydrogen and / or oxygen.

In order to achieve the above object, the apparatus according to the embodiment of the present invention heats water (H ₂ O) to decompose hydrogen and oxygen gas by high temperature, extract the decomposed gas, and extract a part of the extracted gas. The heat of decomposition can be reused for the decomposition of the water and used for the decomposition of the water.

In the present invention, the high temperature at which the water is decomposed into hydrogen and oxygen may be 550 degrees Celsius or more as the first temperature range.

In the present invention, the hydrogen and oxygen may be further heated to a second temperature range so as to separate and extract the hydrogen and oxygen, so that the hydrogen and oxygen are separated into layers, and the second temperature range is 750 degrees Celsius. The second temperature range may be 850 degrees Celsius or more and 950 degrees or less so that the separation purity of the separated hydrogen and oxygen is high.

According to another embodiment of the present invention, the apparatus includes a reaction tank including a water supply unit to which water is supplied from the outside, a heating unit for heating the reaction tank, and connected to an upper side of the reaction tank to extract hydrogen generated in the reaction tank. It may include a hydrogen extraction tube.

In the present invention, the hydrogen extraction tube may be a hydrogen extraction tube for combustion for use of the generated hydrogen in the combustion of the heat energy generator or a storage hydrogen extraction tube for storing the generated hydrogen in an external reservoir, the heating unit is A combustion furnace configured to penetrate the reaction tank body may include a fuel transfer pipe for supplying fuel into the combustion furnace, and an igniter for igniting the fuel.

In the present invention, a first valve and a second valve may be installed in the combustion hydrogen extraction pipe and the storage hydrogen extraction pipe, respectively, to control whether the extraction pipes are opened or closed. A controller for controlling the operation of the heating unit, the first valve and the second valve according to the temperature may be further included.

In the present invention, the lower side of the reaction tank may further include an oxygen extraction tube for extracting the oxygen generated in the reaction tank, the oxygen extraction tube is for combustion for using the generated oxygen as a combustion of the thermal energy generating device An oxygen extraction tube or a storage oxygen extraction tube for storing the generated oxygen in an external reservoir, wherein the combustion oxygen extraction tube and the storage oxygen extraction tube are respectively controlled by a third valve and a third valve to control the opening and closing of the extraction tubes. Four valves can be installed.

In the present invention, it may further include a temperature sensor for measuring the temperature inside the reaction tank and delivers to the controller, the thermal energy generating device is connected to the side of the reaction tank for supplying water and the control of the controller And a fifth valve for controlling whether the water supply pipe is opened or closed, and further comprising a pressure sensor for measuring the pressure inside the reaction tank and transmitting the pressure to the controller. The opening and closing amount of the fifth valve can be adjusted.

The fifth valve of the present invention may be a check valve for preventing the back flow so that the gas inside the reaction tank does not flow back by the pressure of the reaction tank.

In addition, in the present invention, the controller may block the supply of fuel supplied through the fuel delivery pipe when the first valve is opened.

In the present invention, the controller may open the first valve when the temperature inside the reaction tank measured by the temperature sensor is 750 degrees Celsius or more, the second range temperature.

The controller of the present invention may open the second valve when the temperature inside the reaction tank is 850 degrees Celsius or more by the temperature sensor.

In the present invention, a cooler for cooling the hot hydrogen to be transported may be connected to one side of the storage hydrogen extraction pipe.

In addition, one end of the water supply pipe may be connected to the water reservoir for storing the water to be forcibly supplied by the pump at a certain level.

In the present invention, the heat energy generating device casing may be installed standing in the vertical direction. The upper portion of the heat energy generating device may further include a cover for discharging the heat of combustion to the outside, the cover is a heat insulating cap covering the upper portion of the reaction tank, the upper portion of the heat in the combustion heat is insulated for thermal insulation of the reaction tank The lid is mounted, and the top of the heat insulating lid may be equipped with a control lid which is adjusted in height to adjust the discharge of the heat of combustion.

In the present invention, the thermal energy generating device may further include a control valve that operates to discharge the gas in the reaction tank to the outside by a pressure sensor when the pressure in the reaction tank is more than a predetermined pressure.

In the present invention, the safety valve (safty) to operate so that the gas inside the reaction tank is discharged to the outside by a pressure sensor when the pressure inside the reaction tank is more than a predetermined pressure even when the control valve is operated. valve may be further included.

In the present invention, the hydrogen extraction tube, the oxygen extraction tube, the water light pipe, the igniter may be installed to each temperature sensor to operate only at a predetermined temperature or more.

According to the present invention, hydrogen and oxygen which are useful resources can be obtained by pyrolyzing water which is easy to handle and obtain.

In addition, according to the present invention it is possible to supply energy by burning the extracted hydrogen and / or oxygen.

1 is a side cross-sectional view of a thermal energy generating device according to a first embodiment of the present invention.

FIG. 2 illustrates a state in which fuel and water are supplied to FIG. 1.

3 illustrates a state in which water vapor is formed inside the reaction tank in FIG. 1.

4 illustrates a state in which hydrogen for combustion is supplied in FIG. 1.

FIG. 5 illustrates a state in which hydrogen and oxygen for storage are extracted in FIG. 1.

6 is a side sectional view of a heat energy generating device according to a second embodiment of the present invention.

7 is an external view of a horizontal casing of an embodiment of the present invention.

8 is an exploded view of the vertical casing according to the application of the present invention.

9 is a vertical casing coupling of FIG.

10 is a vertical casing installation state of FIG.

100,200,300: thermal energy generator 110,210,310: casing

120,220,320: reaction tanks 130,230,330: combustion furnace

140,240,340: hydrogen extraction pipe for combustion 142,242,342: hydrogen extraction pipe for storage

144,244,344: oxygen extraction pipe for storage 150,250,350: fuel transport pipe

152,252,352: igniter 160,260,360: water supply pipe

In the following, embodiments of the present invention are described with reference to the accompanying drawings.

In the following description of the present invention, if it is determined that detailed descriptions of related known functions or configurations may unnecessarily obscure the subject matter of the present invention, the detailed description will be omitted. In addition, the terms to be described later are terms set in consideration of functions in the present invention, and these terms may vary according to the intention or custom of the producer producing the product, and the definition of the terms should be made based on the contents throughout the present specification.

(First embodiment)

First, a gas extraction and thermal energy generating apparatus according to high temperature decomposition of water according to a first embodiment of the present invention will be described with reference to FIG. 1.

As shown in Figure 1, the gas extraction and thermal energy generating apparatus 100 according to the high temperature decomposition of water according to the first embodiment (100: for convenience of description, hereinafter, unless otherwise stated, 'gas extraction according to high temperature decomposition of water) And the 'heat energy generator' is briefly referred to as a 'heat energy generator', and the casing 110 constitutes an appearance of the heat energy generator 100.

The reaction tank 120 is installed in the inner space of the casing 110, and a combustion furnace 130 penetrating the body is formed.

The heating unit is coupled to one side of the reaction tank 120 to heat the reaction tank 120. The heating unit includes a fuel transfer pipe 150 for supplying fuel into the combustion furnace 130 and an igniter 152 for igniting the fuel. At this time, the fuel used is preferably diesel or LPG, but it is not limited thereto. Of course, general fossil fuel may be used.

Note that the igniter 152 ignites the fuel supplied as fuel during the initial operation, and then ignites the hydrogen when hydrogen is supplied through the combustion hydrogen extraction pipe 140.

The hydrogen extraction pipe 140 for combustion is connected to the other upper side of the reaction tank 120 to transfer the hydrogen generated in the reaction tank 120 to the combustion furnace 130.

The first valve 141 controls whether the combustion hydrogen extraction pipe 140 is opened or closed under the control of the controller.

The storage hydrogen extraction pipe 142 is connected to an upper side of the reaction tank 120 to transfer the hydrogen generated in the reaction tank 120 to a hydrogen storage tank (not shown).

The second valve 143 controls whether the storage hydrogen extraction pipe 142 is opened or closed under the control of the controller.

The storage oxygen extraction pipe 144 is connected to one lower side of the reaction tank 120 to transfer oxygen generated in the reaction tank 120 to an oxygen storage tank (not shown).

The fourth valve 145 controls whether the storage oxygen extraction pipe 144 is opened or closed under the control of the controller.

The water supply pipe 160 is connected to the side of the reaction tank 120 to supply water.

The fifth valve 161 controls whether the water supply pipe 160 is opened or closed under the control of the controller. On the other hand, it is preferable that the fifth valve 151 uses a check valve for preventing a back flow so that the gas inside the reaction tank does not flow back due to the pressure of the reaction tank.

The temperature sensor 122 measures the temperature inside the reaction tank 120 and transmits the temperature to the controller.

The pressure sensor 124 measures the pressure inside the reaction tank 120 and transmits the pressure to the controller.

A controller (not shown) controls the operation of the heater and valves in accordance with the temperature or pressure inside the reaction tank 120.

Hereinafter, the operation of the heat energy generator according to the first embodiment will be described with reference to FIGS. 2 to 5.

FIG. 2 illustrates a state in which fuel and water are supplied from FIG. 1, FIG. 3 illustrates a state in which water vapor is formed inside the reaction tank in FIG. 1, and FIG. 4 is a state in which hydrogen for combustion is supplied in FIG. 1. 5 shows a state in which hydrogen and oxygen for storage are extracted in FIG. 1.

In the first step, the fuel 155 transferred through the fuel transfer pipe 150 is supplied to the combustion furnace 130 and ignited by the igniter 152. At the same time, the fifth valve 161 is opened so that the water 165 transferred through the water supply pipe 160 is supplied into the reaction tank 120. The state at this time is shown in FIG.

In the second step, the reaction tank 120 is heated by the combustion heat of the fuel complexed in the combustion furnace 130, whereby the water 165 supplied into the reaction tank 120 becomes the steam 166.

When the set temperature and pressure conditions are reached, the fifth valve 161 is closed. At this time, the temperature inside the reaction tank 120 is more than 100 degrees Celsius, and as the water 165 becomes water vapor 166, the internal pressure increases. The state at this time is shown in FIG.

In the third step, when the temperature inside the reaction tank 120 becomes higher than 600 degrees Celsius due to the heat of combustion of the fuel ignited in the combustion furnace 130, the steam 166 is pyrolyzed, and the upper portion of the reaction tank 120 is relatively Hydrogen 167 having a low specific gravity is produced and oxygen 168 having a large specific gravity is produced at the lower portion.

When the reaction tank 120 is further heated at the time when hydrogen and oxygen are decomposed, and the temperature inside the tank is 750 degrees Celsius or more, since most of the decomposed hydrogen and oxygen are separated from the upper and lower layers, the decomposed hydrogen can be discharged. Done.

That is, the generated hydrogen 167 is transferred to the combustion furnace 130 through the hydrogen extraction pipe 140 for combustion as the first valve 141 is opened, and is ignited by the igniter 152 to react with the reaction tank 120. ) Is used to heat.

At this time, the fuel delivery pipe 150 cuts off the fuel supply under the control of the controller. In addition, water is supplied through the water supply pipe 160 such that the pressure inside the reaction tank 120 is constant by the pressure sensor 124, and the supplied water is immediately pyrolyzed. The state at this time is shown in FIG.

In the fourth step, when the temperature inside the reaction tank 120 becomes higher than 850 degrees Celsius due to the combustion heat of hydrogen complexed in the combustion furnace 130, the second valve 143 is opened to store the hydrogen extraction pipe 142. Through the pure water of high purity is transferred to the hydrogen storage tank. The state at this time is shown in FIG. On the other hand, since such combustion is performed using hydrogen and oxygen, no separate exhaust gas or pollutants are emitted, and only water is generated, so that it does not cause environmental pollution.

Second Embodiment

Hereinafter, a heat energy generating device according to a second embodiment of the present invention will be described with reference to FIG. 6.

As shown in FIG. 6, the heat energy generator 200 according to the second embodiment of the present invention is compared with the heat energy generator 100 according to the first embodiment of the combustion oxygen extraction pipe 246 and the fourth valve 247. ) Are substantially the same except that they are further combined.

The combustion oxygen extraction tube 246 is connected to the other lower side of the reaction tank 220 to transfer the oxygen generated in the reaction tank 220 to the combustion furnace 230. The fourth valve 247 controls whether the combustion oxygen extraction tube is opened or closed under the control of the controller.

With such a configuration, the heat energy generator 200 according to the second embodiment can supply oxygen required for combustion of hydrogen without external air.

In the thermal energy generating device according to the embodiment of the present invention as described above, since hydrogen gas of 1,000 rubes (m 3) can be produced in 1 liter of water, 18,000 rubes are produced in 18 liters, of which 200 rubes are consumed. In the end, 17,800 rubes would be produced as a commodity.

Accordingly, the daily output is 432,000 rubes (18,000 × 24 hours), the 30-day output is 12,960,000 rubes (432,000 × 30 days), and the annual output is 155,520,000 rubes (12,960,000 × 12 months). .

Since the daily consumption is 200 rubes, the annual consumption is 1,728,000 rubes.

Thus, the total output of one unit will be 155,520,000-1,728,000 = 153,792,000 rubes, so that one can produce 153,792,000 rubes of hydrogen per year.

On the other hand, the heat energy generating device of the embodiment described when the casing 110 is laid down in a horizontal state as shown in Figure 7, when the casing 110 in a vertical direction to design a large capacity 30 liters of hydrogen production effect It can be further improved.

(Third embodiment)

Hereinafter, a heat energy generator according to a third embodiment of the present invention will be described with reference to FIGS. 8 to 10.

8 is an exploded view of the vertical casing according to the third embodiment of the present invention, FIG. 9 is a vertical casing coupling diagram of FIG. 8, and FIG. 10 is a vertical casing installation state of FIG. 8.

The vertical thermal energy generator 300 is installed by standing the casing 310 in a vertical direction as shown in FIGS. 8 to 10, and a combustion tank penetrating the body in the reaction tank 320 installed in the inner space. 330 is formed, the heat insulating cap 370 is mounted on the upper portion and the heat insulating lid 380 is flowed by the heat of combustion discharged through the combustion furnace 330 on the upper portion of the heat of the combustion can be controlled The adjusting lid 380 is configured to be seated.

In addition, a heating unit including a fuel transfer pipe 350 and an igniter 352 is configured at a lower portion thereof, and a combustion hydrogen extraction pipe 340 for supplying hydrogen generated in the reaction tank 320 is provided at one side. .

On the other hand, one side of the casing 310 is provided with a water tank 362 for storing the water to be transmitted through the water supply pipe 360 to the reaction tank 320, the water tank 363 is composed of a glass tube with a scale of water It is desirable to allow consumption to be checked.

And the storage hydrogen extraction pipe 342 for transferring the hydrogen generated in the reaction tank 320 to the hydrogen storage tank (not shown) is configured to be connected, one end of the storage hydrogen extraction pipe 342 As in 10, the three coolers 390 are configured to be sequentially connected to cool the high temperature hydrogen.

In addition, the lower one side of the reaction tank 320 can be confirmed that the storage oxygen extraction pipe 344 for connecting the oxygen generated therein to the oxygen storage tank (not shown) is configured. Likewise, one or more coolers (not shown) capable of cooling high temperature oxygen may be included.

On the other hand, reference numeral 301 is a control valve (control valve), when the pressure inside the reaction tank 320 is more than a predetermined pressure by a pressure sensor (not shown) the control valve 301 is opened while the reaction tank Oxygen in 320 is discharged to the outside.

In addition, 302 is a safety valve (safty valve), when the pressure control in the reaction tank 320 is not possible to control even when the control valve is open, the safety valve to prevent accidents such as tank explosion due to high pressure Is opened to allow the gas inside the reaction tank 320 to be discharged to the outside.

In addition, the temperature sensor (303, 304, 305, 306) is mounted to the combustion hydrogen extraction pipe 340, the storage oxygen extraction pipe 344, the water supply pipe 360, the igniter 352, respectively, the hydrogen extraction pipe, The valve mounted on the water supply pipe and the oxygen extraction pipe is configured to open.

Of course, the storage hydrogen extraction tube 342, the combustion oxygen extract tube 346 may be equipped with a temperature sensor.

In addition, when the predetermined temperature is above, the igniter is turned off so that the temperature sensor is mounted on the igniter so that the reactor itself stops operating.

In the vertical heat energy generating device having such a configuration, while the fuel transported and supplied through the fuel transport pipe 350 is ignited by the igniter 352, the water stored in the water tank 362 is pumped by the water supply pipe. It is supplied into the reaction tank 320 through 360.

At this time, the reaction tank 320 is heated by the combustion heat of the fuel ignited in the combustion furnace 330, and the internal pressure increases as the supplied water changes to a vapor state, thereby increasing hydrogen and oxygen due to a difference in pyrolysis specific gravity of water vapor. Will be created.

Subsequently, the hydrogen completely separated by continuous heating is moved downward through the hydrogen extraction pipe 340 for combustion and then ignited by the igniter 352 to continuously heat the reaction tank 320. .

Further, pure hydrogen having high purity is continuously transferred through the storage hydrogen extraction pipe 342 to be cooled in the cooler 390 and then stored in the hydrogen storage tank by the continuous heating action.

On the other hand, the oxygen generated in the reaction tank 320 is transferred to the lower through the combustion oxygen extraction pipe 346 is used for the ignition action by the igniter 352, the high purity oxygen is a separate storage oxygen extraction pipe Transferred through 344 may be stored in an oxygen storage tank (not shown).

In the vertical thermal energy generating device of the present application as described above, since 1000 liters of hydrogen gas (m 3) can be produced in 1 liter of water, 30,000 rubes are produced in 30 liters, of which 300 rubes are consumed, Eventually 29,700 rubes will be produced as a commodity.

Accordingly, it can be seen that the daily output is 720,000 rubes (30,000 × 24 hours), the 30-day output is 21,600,000 rubes (720,000 × 30 days), and the annual output is 259,200,000 rubes (22,600,000 × 12 months). .

And since the daily consumption is 300 rubes, the annual consumption is 2,592,000 rubes.

Therefore, the total output of one unit is 259,200,000-2,592,000 = 256,608,000 rubes, so it can be seen that one generation can produce 256,608,000 rubes of hydrogen per year.

The embodiments of the present invention have been described above with reference to the accompanying drawings.

However, it is to be noted that the present invention is not particularly limited only to the above-described embodiments, and that various modifications and changes can be made by those skilled in the art within the spirit and spirit of the appended claims as necessary.

Claims

Heat water (H 2 O) to decompose hydrogen and oxygen gas by high temperature, extract the decomposed gas, reuse some of the extracted gas for the decomposition of water, and use the heat of decomposition used for decomposition of water Gas extraction and thermal energy generator according to the high temperature decomposition of H 2 O, characterized in that used as.
The method of claim 1, wherein the water is decomposed into hydrogen and oxygen has a high temperature that the first temperature range occurs gas extraction and thermal energy according to a high temperature of decomposition, H 2 O, characterized in that not less than 550 ° C as the device.
3. The high temperature of H 2 O according to claim 2, wherein the hydrogen and oxygen are further heated to a second temperature range so that the hydrogen and oxygen can be separated and extracted to separate the hydrogen and oxygen. Gas extraction and thermal energy generator according to decomposition.
According to claim 3, wherein the second temperature range is 750 degrees Celsius or more, gas extraction and heat energy generating apparatus according to the high-temperature decomposition of H 2 O.
The gas extraction and thermal energy generator according to the high-temperature decomposition of H 2 O, characterized in that the secondary temperature range is 850 degrees Celsius or more and 950 degrees or less so that the separation purity of the separated hydrogen and oxygen is high. .
According to any one of claims 1 to 5 in order to generate gas extraction and thermal energy due to the high temperature decomposition of H 2 O,

A reaction tank including a water supply unit to which water is supplied from the outside;

A heating unit for heating the reaction tank;

Gas extraction and thermal energy generating device according to the high temperature decomposition of H 2 O, characterized in that it comprises a hydrogen extraction tube that is connected to the upper side of the reaction tank to extract the hydrogen produced in the reaction tank.
The method of claim 6, wherein the hydrogen extraction tube is characterized in that the hydrogen extraction tube for combustion for use of the generated hydrogen in the combustion of the heat energy generator or a storage hydrogen extraction tube for storing the generated hydrogen in an external reservoir, Gas extraction and thermal energy generator according to high temperature decomposition of H 2 O.
8. The apparatus of claim 7, wherein the heating unit comprises: a combustion furnace formed to penetrate the reaction tank body;

A fuel delivery pipe for supplying fuel into the combustion furnace; And

And an igniter for igniting the fuel. 2 .
The method of claim 6, wherein the combustion hydrogen extraction pipe and the storage hydrogen extraction pipe, characterized in that the first valve and the second valve is installed so as to control whether the extraction pipe opening and closing, H 2 O of Gas extraction and thermal energy generator according to high temperature decomposition.
10. The high temperature of H 2 O according to claim 9, wherein the thermal energy generator further comprises a controller for controlling the operation of the heating unit, the first valve, and the second valve according to a temperature inside the reaction tank. Gas extraction and thermal energy generator according to decomposition.
The method of claim 10, wherein the lower side is generated in the gas extraction and thermal energy according to a high temperature of decomposition, H 2 O, characterized in that it further comprises an oxygen-extracting pipe unit for extracting the oxygen produced in the reaction tank, the reaction tank.
12. The method of claim 11, wherein the oxygen extraction tube is a combustion oxygen extraction tube for using the generated oxygen as a combustion of the heat energy generator or a storage oxygen extraction tube for storing the generated oxygen in an external reservoir, Oxygen extraction tube and the storage oxygen extraction tube is characterized in that the third valve and the fourth valve is installed to control the opening and closing of the extraction tube, respectively, gas extraction and heat energy generation according to the high temperature decomposition of H 2 O Device.
The method of claim 9, wherein said reaction tank to measure the internal temperature of the gas extraction and thermal energy generating device according to the temperature sensor, the high-temperature decomposition of H 2 O, characterized in that it further comprises passing to the controller.
The apparatus of claim 13, wherein the thermal energy generator includes a water supply pipe connected to the side of the reaction tank to supply water, and a fifth valve controlling whether the water supply pipe is opened or closed under the control of a controller.

Further comprising; a pressure sensor for measuring the pressure inside the reaction tank to deliver to the controller,

Wherein the controller is characterized in that for adjusting the opening and closing amount of the fifth valve so that the pressure inside the reaction tank, H 2 O gas extraction and thermal energy generator according to the high temperature decomposition.
15. The method of claim 14, wherein the fifth valve is a check valve for preventing the back flow of the gas inside the reaction tank by the pressure of the reaction tank, characterized in that the gas extraction and heat energy generation according to the high-temperature decomposition of H 2 O Device.
11. The method of claim 10, wherein the controller of the first valve when the opening, characterized in that to stop the supply of fuel supplied through the fuel feed tube, the extraction gas of the high temperature decomposition of H 2 O, and heat energy generating device .
14. The method of claim 13, wherein said controller when the temperature inside the reaction tank measured by the temperature sensor and the second order temperature range in ° C 750 or more, comprising a step of opening the first valve, H 2 Gas extraction and thermal energy generator according to high temperature decomposition of O.
14. The method of claim 13, wherein the controller is extracted gas according to a high-temperature decomposition of, H 2 O, characterized in that for the temperature in the reaction tank by the temperature sensor opening, the second valve is above 850 ° C and Thermal energy generator.
The method of claim 7, wherein the heat generator casing is gas extraction, and thermal energy generating device according to the high temperature decomposition of the upright in the vertical direction, characterized in the installed, H 2 O.
The gas extraction and thermal energy generating device according to the high temperature decomposition of H 2 O, characterized in that a cooler for cooling the high temperature hydrogen to be transported is connected to one side of the storage hydrogen extraction pipe.
The gas extraction and thermal energy generating device according to the high-temperature decomposition of H 2 O according to claim 14, characterized in that the water supply pipe is connected to one end of the water reservoir for storing the water to be forcibly supplied by a pump.
22. The apparatus for extracting gas and generating heat energy according to high-temperature decomposition of H 2 O according to claim 21, wherein a glass tube is formed on one side of the bucket so as to measure the consumption of water from the outside.
The method of claim 7, wherein the thermal energy generating device, the upper combustion gas extraction and thermal energy generator according to the high temperature decomposition of, H 2 O, characterized in that further comprises cover that can be discharged to the outside.
24. The method of claim 23, wherein the cover is a heat insulating cap covering the upper portion of the reaction tank, the heat of combustion is mounted on top of the heat energy generating device is a heat insulating cap for the insulation of the reaction tank, the heat insulating cap is to control the emission of combustion heat Gas extraction and heat energy generating device according to the high-temperature decomposition of H 2 O, characterized in that the height is adjusted so that the control lid is mounted.
According to claim 7, wherein the thermal energy generating device further comprises a control valve that operates to discharge the gas in the reaction tank to the outside by a pressure sensor when the pressure in the reaction tank is a predetermined pressure or more. Gas extraction and thermal energy generator according to the high-temperature decomposition of H 2 O.
The safety valve of claim 25, wherein the control valve is operated so that the gas inside the reaction tank is discharged to the outside by a pressure sensor when the pressure inside the reaction tank becomes equal to or greater than a predetermined pressure. (Safty valve) further comprising, gas extraction and thermal energy generator according to the high temperature decomposition of H 2 O.
15. The method of claim 14, wherein the hydrogen extraction tube, oxygen extraction tube, water light pipe, the igniter is a temperature sensor is installed to operate only at a predetermined temperature, respectively, gas extraction and thermal energy due to high temperature decomposition of H 2 O Generator.