Hydrogen atom reaction steam method

Abstract

The invention discloses a hydrogen atom reaction steam method which is characterized by comprising the following steps: S1, controlling each gas electromagnetic valve on a gas pipeline to be opened, enabling the gas pipeline to form a passage, vacuumizing the gas pipeline at least twice, ensuring that oxygen-containing gas does not exist in the gas pipeline, and closing the opened gas electromagnetic valve; s2, adding a proper amount of H2 and H2S into a hydrogen storage tank, adding a proper amount of a catalyst R into a catalytic chamber 36, and adding a proper amount of water into a hydrogen atom reaction steam generator and a water replenishing tank; and S3, each electromagnetic valve on the gas pipeline is controlled to be opened, and the opening degree of each electromagnetic valve is controlled. The invention relates to the technical field of heat energy engineering, in particular to a hydrogen atom reaction steam method. The technical problem to be solved by the invention is to provide the hydrogen atom reaction steam method, heat is generated by hydrogen cycle decomposition reaction, the steam cost is reduced, and the environmental pollution emission is almost zero.

Description

Technical Field

[0001] The invention relates to the technical field of thermal energy engineering, in particular to a hydrogen atom reaction steam method. Background Art

[0002] The system we launched is based on the catalytic decomposition of hydrogen molecules to produce hydrogen atoms, which react exothermically to recombine into hydrogen molecules, which are then recycled to produce steam continuously. When the equipment is operating normally, the equipment relies on the heat generated by itself to maintain the process energy input of the system, and the hydrogen molecules achieve closed-loop circulation, which greatly reduces the cost of steam.

[0003] The system has shortcomings and solutions:

[0004] 1. It can only produce saturated steam and other forms of superheaters can be added.

[0005] 2. The production requirements are very high. All equipment must have reliable technical guarantees and no leakage. Improve the design standards and increase effective control and testing of the production process to fully meet the design requirements.

[0006] 3. In addition, the control process must be reliable. The safety of the equipment is mainly reflected in the electrical control, which is the core of the equipment. If each temperature point and pressure point want to meet the process requirements, it is necessary to achieve precise control of the key points, otherwise the reaction will be uncontrollable and uncontrollable safety will occur. The electrical design must be controlled by PLC, and the entire control must have safety emergency control.

[0007] 4. The last point is that the equipment manufacturing cost is high, the equipment structure is relatively complex, and the equipment standard requirements are high. To reduce the cost, it is necessary to rely on production to make up for it, and at the same time, to achieve standardized design of the equipment. Summary of the invention

[0008] The technical problem to be solved by the present invention is to provide a hydrogen atom reaction steam method, which utilizes hydrogen cyclic decomposition reaction to generate heat, reduces steam costs, and has almost zero environmental pollution emissions.

[0009] The present invention adopts the following technical solutions to achieve the invention objectives:

[0010] A hydrogen atom reaction steam method, characterized in that it comprises the following steps:

[0011] S1: Control each gas solenoid valve on the gas pipeline to open, so that the gas pipeline forms a passage, vacuumize the gas pipeline, vacuumize at least twice, ensure that there is no oxygen-containing gas in the gas pipeline, and close the opened gas solenoid valve;

[0012] S2: Add appropriate amount of H2 and H2S into the hydrogen storage tank, add appropriate amount of catalyst R into the catalyst chamber 36, and add appropriate amount of water into the hydrogen atom reaction steam generator and the water supply tank;

[0013] S3: Control each solenoid valve on the gas pipeline to open, and control the opening degree of each solenoid valve;

[0014] S4: The hydrogen compressor compresses the gas in the hydrogen storage tank and transports it to the pressure buffer tank to achieve pressure buffering;

[0015] S5: The electric regulating valve delivers the mixed gas to the heater, and the gas is heated to 310° by the heater, and part of the hydrogen sulfide is decomposed into H atoms and HS free radicals;

[0016] S6: The mixed gas is transported into the catalyst chamber, the catalyst R reacts with H atoms to generate RH, and H2 and H2S react with the catalyst R to generate H atoms;

[0017] S7: A mixed gas of H2, a large number of H atoms, HS free radicals and H2S enters the hydrogen atom reaction steam generator, two H atoms are combined into a hydrogen molecule, and then a large amount of heat is released, and the heat is released in the form of steam through the hydrogen atom reaction steam generator, and the H atoms and HS free radicals generate H2S;

[0018] S8: H2 and H2S enter the gas pipeline in the water supply tank to heat the water in the water supply tank and realize secondary release of heat;

[0019] S9: H2 and H2S return to the hydrogen storage tank;

[0020] S10: When the amount of water in the hydrogen atom reaction steam generator is small, the water replenishing tank works to transport the water in the water replenishing tank to the hydrogen atom reaction steam generator through the liquid pipeline.

[0021] As a further limitation of the present technical solution, the gas pipeline includes the hydrogen storage tank, the hydrogen compressor, the pressure buffer tank, the heater, the catalyst chamber, the hydrogen atom reaction steam generator and the water replenishment tank, the gas outlet end of the hydrogen storage tank is fixedly connected to the main gas outlet pipe, the main gas outlet pipe is fixedly connected to the gas inlet end of the hydrogen compressor, the gas outlet end of the hydrogen compressor is fixedly connected to the pressurized gas pipe, the pressurized gas pipe is fixedly connected to the gas inlet end of the pressure buffer tank, the gas outlet end of the pressure buffer tank is fixedly connected to the decompression gas pipe, and the decompression gas pipe is fixedly connected to the heater The air inlet end of the heater is fixedly connected to the heating air pipe, the heating air pipe is fixedly connected to the air inlet end of the catalyst chamber, the air outlet end of the catalyst chamber is fixedly connected to the gas pipeline inlet of the hydrogen atom reaction steam generator, the gas pipeline outlet of the hydrogen atom reaction steam generator is fixedly connected to the cooling air pipe, the cooling air pipe is fixedly connected to the gas pipeline inlet of the water replenishing tank, the gas pipeline outlet of the water replenishing tank is fixedly connected to the return air pipe, the return air pipe is fixedly connected to the air inlet end of the hydrogen storage tank, and a flow valve and an electric regulating valve are installed on the pressure reducing air pipe.

[0022] As a further limitation of the present technical solution, the liquid pipeline includes the hydrogen atom reaction steam generator and the water replenishing tank, the hydrogen atom reaction steam generator and the water replenishing tank are respectively fixedly connected to water pipes, and a water pump is installed on the water pipes.

[0023] As a further limitation of the present technical solution, a gas solenoid valve is installed on the gas pipeline, a cooling gas pipe outlet valve and a water supply tank gas coil inlet valve are installed on the cooling gas pipe, a water supply tank gas coil outlet valve and a return gas pipe outlet valve are installed on the return gas pipe, a main gas outlet pipe inlet valve and a main gas outlet pipe outlet valve are installed on the main gas outlet pipe, a pressure buffer tank output valve is installed on the pressure reducing gas pipe, a heating gas pipe inlet valve is installed on the heating gas pipe, and a heating gas pipe outlet valve is installed on the heating gas pipe.

[0024] As a further limitation of the technical solution, a liquid solenoid valve is installed on the liquid pipeline, and a water pipe inlet valve and a water pipe outlet valve are installed on the water pipe.

[0025] As a further limitation of the present technical solution, it also includes a monitoring component, wherein a cooling air pipe pressure sensor and a cooling air pipe temperature sensor are installed on the cooling air pipe, a return air pipe pressure sensor and a return air pipe temperature sensor are installed on the return air pipe, a hydrogen storage tank temperature sensor and a hydrogen storage tank pressure sensor are installed in the hydrogen storage tank, a pressure buffer tank temperature sensor and a pressure buffer tank pressure sensor are installed in the pressure buffer tank, and a heating air pipe temperature sensor and a heating air pipe pressure sensor are installed on the heating air pipe.

[0026] As a further limitation of the technical solution, a steam pressure sensor and a steam temperature sensor are installed in the hydrogen atom reaction steam generator, and a make-up water temperature sensor and a water tank pressure sensor are installed in the make-up water tank.

[0027] As a further limitation of the technical solution, a liquid level sensor is installed on the upper part of the hydrogen atom reaction steam generator.

[0028] As a further limitation of the present technical solution, the catalyst chamber is installed at the lower part of the hydrogen atom reaction steam generator.

[0029] As a further limitation of the present technical solution, the catalyst is a non-oxygen-containing catalyst.

[0030] Compared with the prior art, the advantages and positive effects of the present invention are:

[0031] 1. This device uses hydrogen cycle decomposition reaction to generate heat, and the raw materials are not consumed. Therefore, the steam cost is very low, far less than the cost of coal burning, and the environmental pollution emission is almost zero, with huge economic and social benefits.

[0032] 2. This device uses sensors and other equipment in conjunction with electrical control to adjust the steam output, automatically track and control the reaction speed, truly realize intelligent steam regulation, and achieve worry-free production scheduling for different users. BRIEF DESCRIPTION OF THE DRAWINGS

[0033] Figure 1 It is a schematic diagram of the process of the present invention.

[0034] Figure 2 The structure of the present invention is schematically shown Figure 1 .

[0035] Figure 3 The structure of the present invention is schematically shown Figure 2 .

[0036] In the figure: 1. Steam pressure sensor, 2. Steam temperature sensor, 3. Hydrogen atomic reaction steam generator, 4. Cooling air pipe outlet valve, 5. Cooling air pipe pressure sensor, 6. Cooling air pipe temperature sensor, 7. Cooling air pipe, 8. Water supply tank gas coil inlet valve, 9. Water supply water temperature sensor, 10. Water supply tank, 11. Water tank pressure sensor, 12. Water supply tank gas coil outlet valve, 13. Return air pipe pressure sensor, 14. Return air pipe temperature sensor, 15. Return air pipe, 16. Return air pipe check valve, 17. Return air pipe outlet valve, 18. Hydrogen storage tank, 19. Main outlet pipe, 20. Main outlet pipe outlet valve, 21. Hydrogen compressor, 22. Pressurized air pipe, 23. Pressurized air pipe check valve, 24. Pressure buffer tank, 25. Pressure buffer tank temperature sensor, 26. Pressure 1. Pressure buffer tank output valve, 27. Pressure buffer tank pressure sensor, 28. Pressure reducing air pipe, 29. Pressure reducing air pipe check valve, 30. Heater, 31. Heating air pipe inlet valve, 32. Heating air pipe, 33. Heating air pipe pressure sensor, 34. Flow valve, 35. Electric regulating valve, 36. Catalytic chamber, 37. Liquid level sensor, 38. Heating air pipe temperature sensor, 39. Water pipe outlet valve, 40. Water pipe, 41. Water pipe check valve, 42. Heating air pipe outlet valve, 43. Water pump, 44. Water pipe inlet valve, 45. Hydrogen storage tank pressure sensor, 46. Main air outlet pipe inlet valve, 47. Hydrogen storage tank temperature sensor, 48. Steam pipe inlet valve, 49. Steam pipe, 50. Steam pipe electric regulating valve, 51. Steam pipe outlet valve, 52. Steam distributor. DETAILED DESCRIPTION

[0037] A specific implementation of the present invention is described in detail below in conjunction with the accompanying drawings, but it should be understood that the protection scope of the present invention is not limited by the specific implementation.

[0038] The present invention comprises the following steps:

[0039] S1: Control each gas solenoid valve on the gas pipeline to open, so that the gas pipeline forms a passage, vacuumize the gas pipeline, vacuumize at least twice, ensure that there is no oxygen-containing gas in the gas pipeline, and close the opened gas solenoid valve;

[0040] S2: Add appropriate amount of H2 and H2S into the hydrogen storage tank 18, add appropriate amount of catalyst R into the catalyst chamber 36, and add appropriate amount of water into the hydrogen atom reaction steam generator 3 and the water supply tank 10;

[0041] S3: Control each solenoid valve on the gas pipeline to open, and control the opening degree of each solenoid valve;

[0042] S4: The hydrogen compressor 21 compresses the gas in the hydrogen storage tank 18 and transports it to the pressure buffer tank 24 to achieve pressure buffering;

[0043] S5: The electric regulating valve 35 delivers the mixed gas to the heater 30, and the gas is heated to 310° by the heater 30, and part of the hydrogen sulfide is decomposed into H atoms and HS free radicals;

[0044] S6: The mixed gas is transported into the catalyst chamber 36, the catalyst R reacts with H atoms to generate RH, and H2 and H2S react with the catalyst R to generate H atoms;

[0045] S7: A mixed gas of H2, a large number of H atoms, HS free radicals and H2S enters the hydrogen atom reaction steam generator 3, two H atoms are combined into a hydrogen molecule, and then a large amount of heat is released, and the heat is released in the form of steam through the hydrogen atom reaction steam generator 3, and the H atoms and HS free radicals generate H2S;

[0046] The steam enters the steam distributor 52 through the steam pipe 49 to achieve heat distribution;

[0047] S8: H2 and H2S enter the gas pipeline in the water supply tank 10 to heat the water in the water supply tank 10 and realize secondary release of heat;

[0048] S9: H2 and H2S return to the hydrogen storage tank 18;

[0049] S10: When the amount of water in the hydrogen atom reaction steam generator 3 is small, the water replenishment tank 10 works to transport the water in the tank to the hydrogen atom reaction steam generator 3 through the liquid pipeline.

[0050] The catalyst chamber 36 is an independent device that consumes a certain amount of pressure to reduce the system pressure and thus achieve system pressure balance.

[0051] The key of the whole system is the heater 30 to the output end of the hydrogen atom reaction steam generator 3. Only during this period can the hydrogen atom reaction occur, and it is necessary to ensure that the output end of the hydrogen atom reaction steam generator 3 outputs H2 and H2S. Otherwise, control failure will occur, and the system temperature control and the electric valve cooling air pipe temperature sensor 6, the cooling air pipe outlet valve 4, and the heating air pipe inlet valve 31 form a closed-loop control.

[0052] The temperature in the cooling gas pipe 7 is determined by the steam temperature and is generally about 200°C. The system requires that it should not exceed 300°C.

[0053] Catalysts are mainly used to decompose hydrogen molecules to obtain hydrogen atoms. Two hydrogen atoms are combined into one hydrogen molecule, and then a large amount of heat is released. The heat is released in the form of steam through the hydrogen atom reaction steam generator 3. The hydrogen molecules return to the hydrogen storage tank 18 through cooling, and are then compressed and transported to the pressure buffer tank 24 through the hydrogen compressor 21, and then heated to 310 degrees through the heater 30. The role of this process is that hydrogen sulfide is decomposed into the catalyst chamber 36. Under the action of the solid catalyst, hydrogen atoms are continuously converted and enter the hydrogen atom reaction steam generator 3. The hydrogen atoms are combined into hydrogen molecules after 0.5 seconds to release a large amount of heat, thus forming a closed-loop circulation of hydrogen molecules. The role of hydrogen sulfide and the catalyst in the catalyst chamber 36 is to decompose hydrogen molecules into hydrogen atoms, which are not consumed themselves.

[0054] The gas pipeline includes the hydrogen storage tank 18, the hydrogen compressor 21, the pressure buffer tank 24, the heater 30, the catalyst chamber 36, the hydrogen atom reaction steam generator 3 and the water replenishment tank 10. The gas outlet end of the hydrogen storage tank 18 is fixedly connected to the main gas outlet pipe 19, the main gas outlet pipe 19 is fixedly connected to the gas inlet end of the hydrogen compressor 21, the gas outlet end of the hydrogen compressor 21 is fixedly connected to the pressurized gas pipe 22, the pressurized gas pipe 22 is fixedly connected to the gas inlet end of the pressure buffer tank 24, the gas outlet end of the pressure buffer tank 24 is fixedly connected to the decompression gas pipe 28, and the decompression gas pipe 28 is fixedly connected to the gas inlet end of the heater 30. The outlet end of the heater 30 is fixedly connected to the heating air pipe 32, the heating air pipe 32 is fixedly connected to the air inlet end of the catalyst chamber 36, the outlet end of the catalyst chamber 36 is fixedly connected to the gas pipeline inlet of the hydrogen atom reaction steam generator 3, the gas pipeline outlet of the hydrogen atom reaction steam generator 3 is fixedly connected to the cooling air pipe 7, the cooling air pipe 7 is fixedly connected to the gas pipeline inlet of the water replenishing tank 10, the gas pipeline outlet of the water replenishing tank 10 is fixedly connected to the return air pipe 15, the return air pipe 15 is fixedly connected to the air inlet end of the hydrogen storage tank 18, and a flow valve 34 and an electric regulating valve 35 are installed on the pressure reducing air pipe 28.

[0055] The liquid pipeline includes the hydrogen atom reaction steam generator 3 and the water replenishment tank 10 . The hydrogen atom reaction steam generator 3 and the water replenishment tank 10 are respectively fixedly connected to a water pipe 40 , and a water pump 43 is installed on the water pipe 40 .

[0056] A gas solenoid valve is installed on the gas pipeline, a cooling gas pipe outlet valve 4 and a water replenishing tank gas coil inlet valve 8 are installed on the cooling gas pipe 7, a water replenishing tank gas coil outlet valve 12 and a return gas pipe outlet valve 17 are installed on the return gas pipe 15, a main gas outlet pipe inlet valve 46 and a main gas outlet pipe outlet valve 20 are installed on the main gas outlet pipe 19, a pressure buffer tank output valve 26 is installed on the pressure reducing gas pipe 28, a heating gas pipe inlet valve 31 is installed on the heating gas pipe 32, and a heating gas pipe outlet valve 42 is installed on the heating gas pipe 32.

[0057] A liquid solenoid valve is installed on the liquid pipeline, and a water pipe inlet valve 44 and a water pipe outlet valve 39 are installed on the water pipe 40 .

[0058] It also includes a monitoring component, wherein a cooling air pipe pressure sensor 5 and a cooling air pipe temperature sensor 6 are installed on the cooling air pipe 7, a return air pipe pressure sensor 13 and a return air pipe temperature sensor 14 are installed on the return air pipe 15, a hydrogen storage tank temperature sensor 47 and a hydrogen storage tank pressure sensor 45 are installed in the hydrogen storage tank 18, a pressure buffer tank temperature sensor 25 and a pressure buffer tank pressure sensor 27 are installed in the pressure buffer tank 24, and a heating air pipe temperature sensor 38 and a heating air pipe pressure sensor 33 are installed on the heating air pipe 32.

[0059] The hydrogen atom reaction steam generator 3 is installed with a steam pressure sensor 1 and a steam temperature sensor 2 , and the water supply tank 10 is installed with a water supply temperature sensor 9 and a water tank pressure sensor 11 .

[0060] A liquid level sensor 37 is installed on the upper part of the hydrogen atom reaction steam generator 3 .

[0061] The catalyst chamber 36 is installed at the lower part of the hydrogen atom reaction steam generator 3 .

[0062] The catalyst is a non-oxygen containing catalyst.

[0063] The return air pipe 15 is provided with a return air pipe check valve 16. The pressurized air pipe 22 is provided with a pressurized air pipe check valve 23. The decompression air pipe 28 is provided with a decompression air pipe check valve 29.

[0064] A water pipe check valve 41 is installed on the water pipe 40 .

[0065] The steam output end of the hydrogen atom reaction steam generator 3 is fixedly connected to a steam pipe 49, a steam pipe inlet valve 48 is installed at the input end of the steam pipe 49, a steam pipe outlet valve 51 is installed at the output end of the steam pipe 49, a steam pipe electric regulating valve 50 is installed on the steam pipe 49, and the steam pipe 49 is fixedly connected to a steam distributor 52 to realize steam output.

[0066] The above disclosure is only a specific embodiment of the present invention, but the present invention is not limited thereto, and any changes that can be conceived by those skilled in the art should fall within the protection scope of the present invention.

Claims

1. A hydrogen atom reaction steam method, characterized in that: The following steps are involved: S1: Control each gas solenoid valve on the gas pipeline to open, so that the gas pipeline forms a passage, vacuumize the gas pipeline, and vacuumize it at least twice to ensure that there is no oxygen-containing gas in the gas pipeline, and close the opened gas solenoid valve; S2: adding a proper amount of H2 and H2S into the hydrogen storage tank (18), adding a proper amount of catalyst R into the catalyst chamber (36), and adding a proper amount of water into the hydrogen atom reaction steam generator (3) and the water supply tank (10); S3: Control each solenoid valve on the gas pipeline to open, and control the opening degree of each solenoid valve; S4: The hydrogen compressor (21) compresses the gas in the hydrogen storage tank (18) and transports it to the pressure buffer tank (24) to achieve pressure buffering; S5: The electric regulating valve (35) delivers the mixed gas to the heater (30), and the gas is heated to 310° by the heater (30), and part of the hydrogen sulfide is decomposed into H atoms and HS free radicals; S6: The mixed gas is transported into the catalyst chamber (36), the catalyst R reacts with H atoms to generate RH, and H2 and H2S react with the catalyst R to generate H atoms; S7: A mixed gas of H2, a large number of H atoms, HS free radicals and H2S enters the hydrogen atom reaction steam generator (3), two H atoms are combined into a hydrogen molecule, and then a large amount of heat is released. The heat is released in the form of steam through the hydrogen atom reaction steam generator (3), and the H atoms and HS free radicals generate H2S; S8: H2 and H2S enter the gas pipeline in the water supply tank (10), thereby heating the water in the water supply tank (10) and achieving secondary release of heat; S9: H2 and H2S return to the hydrogen storage tank (18); S10: When the amount of water in the hydrogen atom reaction steam generator (3) is relatively small, the water replenishment tank (10) operates to transport the water in the tank to the hydrogen atom reaction steam generator (3) through a liquid pipeline.

2. The hydrogen atom reaction steam method according to claim 1, characterized in that: The gas pipeline comprises the hydrogen storage tank (18), the hydrogen compressor (21), the pressure buffer tank (24), the heater (30), the catalyst chamber (36), the hydrogen atom reaction steam generator (3) and the water replenishment tank (10); the gas outlet end of the hydrogen storage tank (18) is fixedly connected to the main gas outlet pipe (19); the main gas outlet pipe (19) is fixedly connected to the gas inlet end of the hydrogen compressor (21); the gas outlet end of the hydrogen compressor (21) is fixedly connected to the pressurized gas pipe (22); the pressurized gas pipe (22) is fixedly connected to the gas inlet end of the pressure buffer tank (24); the gas outlet end of the pressure buffer tank (24) is fixedly connected to the decompression gas pipe (28); the decompression gas pipe (28) is fixedly connected to the gas outlet end of the heater (30); The air inlet end and the air outlet end of the heater (30) are fixedly connected to the heating air pipe (32), the heating air pipe (32) is fixedly connected to the air inlet end of the catalyst chamber (36), the air outlet end of the catalyst chamber (36) is fixedly connected to the gas pipeline inlet of the hydrogen atom reaction steam generator (3), the gas pipeline outlet of the hydrogen atom reaction steam generator (3) is fixedly connected to the cooling air pipe (7), the cooling air pipe (7) is fixedly connected to the gas pipeline inlet of the water replenishing tank (10), the gas pipeline outlet of the water replenishing tank (10) is fixedly connected to the return air pipe (15), the return air pipe (15) is fixedly connected to the air inlet end of the hydrogen storage tank (18), and a flow valve (34) and an electric regulating valve (35) are installed on the pressure reducing air pipe (28).

3. The hydrogen atom reaction steam method according to claim 2, characterized in that: The liquid pipeline comprises the hydrogen atom reaction steam generator (3) and the water replenishment tank (10), the hydrogen atom reaction steam generator (3) and the water replenishment tank (10) are respectively fixedly connected to a water pipe (40), and a water pump (43) is installed on the water pipe (40).

4. The hydrogen atom reaction steam method according to claim 3, characterized in that: A gas solenoid valve is installed on the gas pipeline, a cooling gas pipe outlet valve (4) and a water supply tank gas coil inlet valve (8) are installed on the cooling gas pipe (7), a water supply tank gas coil outlet valve (12) and a return gas pipe outlet valve (17) are installed on the return gas pipe (15), a main gas outlet pipe inlet valve (46) and a main gas outlet pipe outlet valve (20) are installed on the main gas outlet pipe (19), a pressure buffer tank output valve (26) is installed on the pressure reducing gas pipe (28), a heating gas pipe inlet valve (31) is installed on the heating gas pipe (32), and a heating gas pipe outlet valve (42) is installed on the heating gas pipe (32).

5. The hydrogen atom reaction steam method according to claim 3, characterized in that: A liquid solenoid valve is installed on the liquid pipeline, and a water pipe inlet valve (44) and a water pipe outlet valve (39) are installed on the water pipe (40).

6. The hydrogen atom reaction steam method according to claim 3, characterized in that: The system also includes a monitoring component, wherein the cooling air pipe (7) is provided with a cooling air pipe pressure sensor (5) and a cooling air pipe temperature sensor (6), the return air pipe (15) is provided with a return air pipe pressure sensor (13) and a return air pipe temperature sensor (14), the hydrogen storage tank (18) is provided with a hydrogen storage tank temperature sensor (47) and a hydrogen storage tank pressure sensor (45), the pressure buffer tank (24) is provided with a pressure buffer tank temperature sensor (25) and a pressure buffer tank pressure sensor (27), and the heating air pipe (32) is provided with a heating air pipe temperature sensor (38) and a heating air pipe pressure sensor (33).

7. The hydrogen atom reaction steam method according to claim 6, characterized in that: The hydrogen atom reaction steam generator (3) is installed with a steam pressure sensor (1) and a steam temperature sensor (2), and the water supply tank (10) is installed with a water supply temperature sensor (9) and a water tank pressure sensor (11).

8. The hydrogen atom reaction steam method according to claim 6, characterized in that: A liquid level sensor (37) is installed on the upper part of the hydrogen atom reaction steam generator (3).

9. The hydrogen atom reaction steam method according to claim 2, characterized in that: The catalyst chamber (36) is installed at the lower part of the hydrogen atom reaction steam generator (3).

10. The hydrogen atom reaction steam method according to claim 1, characterized in that: The catalyst is a non-oxygen containing catalyst.

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