How to implement a green hydrogen generation system

Abstract

To provide a system of generating green hydrogen and green electric power, effectively solving the problem of worldwide climate change and global warming resulting from fossil fuel by generating low-cost green hydrogen and green electric power, and a method of operating the system of generating green hydrogen and green electric power.SOLUTION: The system of generating green hydrogen and green electric power, comprises a raw material mixing unit 1, a separation unit 4, a lightening plasma decomposition unit 5, and a hydrogen energy power generation unit 7. The raw material mixing unit is connected to an external transportation pipe transporting a raw material of a hydrogen production catalyst. The raw material mixing unit is connected to a first hydrolysis reaction unit 2 via the raw material transportation pipe. The first hydrolysis reaction unit is connected to a heat recovery unit 3 via the raw material transportation pipe. The first hydrolysis reaction unit comprises a first heat exchange module 21, and the first heat exchange module and the heat recovery unit are connected to each other via a heat transfer pipe.SELECTED DRAWING: Figure 3

Description

[Technical Field]

[0001] The present invention relates to a green hydrogen generation system, a green power generation system and methods for implementing the green hydrogen and green power generation system. [Background technology]

[0002] Of the many sources of pollution that create the greenhouse effect, carbon dioxide emissions are the most damaging. Carbon dioxide is emitted from fossil fuels, so in order to reduce carbon dioxide emissions, it was necessary to reduce dependence on and use of fossil fuels. The Paris Agreement set out solutions to replace fossil fuels with renewable energy and green hydrogen, but the conventional method of obtaining green hydrogen involves producing it through water electrolysis and using renewable energy sources such as solar and wind power as the power source. As a result, the price of the green hydrogen produced is very high, making it difficult to replace fossil fuels with green hydrogen. Summary of the Invention [Problem to be solved by the invention]

[0003] The main objective of the present invention is to provide a green hydrogen generation system, a green power generation system and an implementation method for the green hydrogen and green power generation system, which can effectively solve the problems of global climate change and global warming caused by fossil fuels by producing cheap green hydrogen and green power. [Means for solving the problem]

[0004] In order to solve the above problems, according to a first aspect of the present invention, there is provided a method for implementing a green hydrogen and green electricity generation system, the green hydrogen and green electricity generation system comprising a raw material mixing unit, a separation unit, an electric light plasma decomposition unit, and a hydrogen energy power generation unit, the raw material mixing unit is connected to a raw material transport pipe of an external hydrogen production catalyst, the raw material mixing unit is connected to a first hydrolysis reaction unit via a raw material transport pipe, the first hydrolysis reaction unit is connected to a heat recovery unit via a raw material transport pipe, the first hydrolysis reaction unit has a first heat exchange module, and the first heat exchange module and the heat recovery unit are connected to each other via a heat transfer tube, the separation unit is connected to the heat recovery unit via a raw material transport pipe, the electric light plasma decomposition unit is connected to the separation unit via a raw material transport pipe, the electric light plasma decomposition unit is connected to a second hydrolysis reaction unit via a raw material transport pipe, the electric light plasma decomposition unit has a second heat exchange module, and the second heat exchange module is connected to the second hydrolysis reaction unit via a heat transfer tube. the hydrogen energy power generation unit is connected to the lightning plasma decomposition unit, the first hydrolysis reaction unit, and the second hydrolysis reaction unit through a raw material transport pipe; the hydrogen energy power generation unit and the second hydrolysis reaction unit are connected to each other through a water supply pipe; the raw material mixing unit and the heat recovery unit are each connected to a water supply pipe connected to an external water source; an external hydrogen production catalyst is transported into the raw material mixing unit through the raw material transport pipe; the external water source supplies water to be transported to the raw material mixing unit through a water supply pipe; the hydrogen production catalyst and water are mixed in the raw material mixing unit; the mixture of the hydrogen production catalyst and water is transported to the first hydrolysis reaction unit through the raw material transport pipe; the mixture of the hydrogen production catalyst and water is hydrolyzed in the first hydrolysis reaction unit to produce hydrogen and a hydrogen oxide production catalyst; and the heat content generated when the hydrogen oxide production catalyst is produced and a large amount of hydrogen production catalyst that has not yet completely reacted are released, and the heat content isThe hydrogen produced by the heat recovery unit and the hydrogen oxide production catalyst are transported to the separation unit through a raw material transport pipe and separated into gaseous green hydrogen and solid hydrogen oxide production catalyst. The hydrogen oxide production catalyst separated by the separation unit is transported to the lightning plasma decomposition unit through a raw material transport pipe and activated, deoxidized, and reduced to produce hydrogen production catalyst. The reduced hydrogen production catalyst is transported to the second hydrolysis reaction unit through a raw material transport pipe and hydrolyzed to produce hydrogen and hydrogen oxide production catalyst. a large amount of heat generated when hydrogen is produced is released, and the heat is transferred to the second heat exchange module installed in the electric plasma decomposition unit through a heat transfer tube and absorbed therein; a hydrogen oxide production catalyst produced in the second hydrolysis reaction unit is transported to the heat recovery unit through a raw material transport pipe and is repeatedly circulated between the heat recovery unit, the separation unit, the electric plasma decomposition unit, and the second hydrolysis reaction unit; the electric plasma decomposition unit reduces the hydrogen oxide production catalyst to produce a hydrogen production catalyst and also produce oxygen, which is transported to the hydrogen energy power generation unit through a raw material transport pipe; hydrogen produced in the first hydrolysis reaction unit and the second hydrolysis reaction unit is transported to the hydrogen energy power generation unit through a raw material transport pipe and produces green electricity and water together with the oxygen transported to the hydrogen energy power generation unit; and the water produced by the hydrogen energy power generation unit is transported to the second hydrolysis reaction unit through a water transport pipe. [Effects of the Invention]

[0005] The green hydrogen generation system, green electricity generation system, and method for implementing the green hydrogen and green electricity generation system of the present invention can obtain the green hydrogen and green electricity used in the system by continuously circulating them while the system is operating, and raw materials such as hydrogen production catalysts and water are recovered and reused within the system, so that inexpensive green hydrogen and green electricity can be obtained, effectively replacing fossil fuels, and solving the problems of global climate change and global warming. [Brief explanation of the drawings]

[0006] [Figure 1] 1 is a block diagram illustrating a green hydrogen production system according to an embodiment of the present invention. [Figure 2] 1 is a block diagram illustrating a green power generation system according to an embodiment of the present invention. [Figure 3] 1 is a block diagram illustrating a green hydrogen and green electricity generation system according to an embodiment of the present invention. [Figure 4] 1 is a cross-sectional view of an electric light plasma decomposition unit according to one embodiment of the present invention; DETAILED DESCRIPTION OF THE INVENTION

[0007] Please refer to Fig. 1. As shown in Fig. 1, a green hydrogen generation system according to one embodiment of the present invention includes a raw material mixing unit 1. The raw material mixing unit 1 is connected to a raw material transport pipe of the external hydrogen production catalyst, the raw material mixing unit 1 and the first hydrolysis reaction unit 2 are connected to each other via a raw material transport pipe, and the first hydrolysis reaction unit 2 and the heat recovery unit 3 are connected to each other via a raw material transport pipe. The first hydrolysis reaction unit 2 has a first heat exchange module 21, and the first heat exchange module 21 and the heat recovery unit 3 are connected to each other via a heat transfer pipe. The green hydrogen production system further comprises a separation unit 4 . The separation unit 4 is connected to the heat recovery unit 3 and the first hydrolysis reaction unit 2 via raw material transport pipes. The raw material mixing unit 1 and the heat recovery unit 3 are each connected to a water pipe connected to an external water source.

[0008] When the green hydrogen generation system of the present invention generates green hydrogen, the external hydrogen production catalyst is transported into the raw material mixing unit 1 through the raw material transport pipe. The hydrogen production catalyst is any one of common metals (also called base metals), metal alloys, metal oxides, and combinations thereof. Metals preferably include copper, iron, aluminum, tin, lead, zinc, sodium, calcium, lithium, potassium, nickel, magnesium, gallium, cadmium, silicon, titanium, and the like. Furthermore, the metal oxide preferably includes copper peroxide (CuO2), iron trioxide (Fe2O3), iron tetroxide (Fe3O4), aluminum oxide (Al2O3), tin dioxide (SnO2), lead dioxide (PbO2), zinc oxide (ZnO), sodium oxide (Na2O), calcium oxide (CaO), lithium oxide (Li2O), potassium oxide (K2O), nickel oxide (Ni2O), magnesium oxide (MgO), gallium oxide (Ga2O3), cadmium oxide (CdO), silicon dioxide (SiO2), titanium dioxide (TiO2), and the like. An external water source supplies water that is transported via a water pipe to the raw material mixing unit 1. The water is pure water. The hydrogen production catalyst and water are mixed uniformly in the raw material mixing unit 1, and the mixture of the hydrogen production catalyst and water is transported to the first hydrolysis reaction unit 2 through the raw material transport pipe. The mixture of the hydrogen production catalyst and water undergoes a water decomposition reaction in the first hydrolysis reaction unit 2 to produce hydrogen and a hydrogen oxide production catalyst. At the same time, a large amount of heat of enthalpy is released when the hydrogen oxide production catalyst is produced, as well as some of the hydrogen production catalyst that has not yet completely reacted. The heat is absorbed by the first heat exchange module 21 installed in the first hydrolysis reaction unit 2 and transported to the heat recovery unit 3 through a heat transfer tube. The hydrogen production catalyst that has not yet completely reacted in the first hydrolysis reaction unit 2 is transported to the heat recovery unit 3 via a raw material transport pipe. The external water source supplies water which is transported to the heat recovery unit 3 through a water supply pipe. The collected heat content and water excite the unreacted hydrogen production catalyst, causing it to react completely and produce hydrogen and hydrogen oxide production catalyst. The hydrogen and hydrogen oxide production catalyst produced by the heat recovery unit 3 and the first hydrolysis reaction unit 2 are then transported to the separation unit 4 through a raw material transport pipe, where they are separated into gaseous green hydrogen and solid hydrogen oxide production catalyst. The green hydrogen can be outputted outside the system via a raw material transport pipe and used for various applications, or the hydrogen oxide production catalyst can be transported outside and used.

[0009] Please refer to Fig. 2. As shown in Fig. 2, the green electricity generating system of the present invention includes an electric light plasma decomposition unit 5. The lightning plasma decomposition unit 5 is connected to a raw material transport pipe for the external hydrogen oxide production catalyst, and the lightning plasma decomposition unit 5 and the second hydrolysis reaction unit 6 are connected to each other via a raw material transport pipe. The lightning plasma decomposition unit 5 has a second heat exchange module 51. The second heat exchange module 51 and the second hydrolysis reaction unit 6 are connected to each other via a heat transfer tube. A water pipe connected to an external water source is connected to the second hydrolysis reaction unit 6. The green electricity generation system of the present invention further includes a hydrogen energy power generation unit . The lightning plasma decomposition unit 5 and the second hydrolysis reaction unit 6 are each connected to a hydrogen energy power generation unit 7 via a raw material transport pipe. The hydrogen energy power generation unit 7 and the second hydrolysis reaction unit 6 are connected to each other via a water pipe. The hydrogen energy power generation unit 7 includes all hydrogen energy source power generation devices, such as hydrogen fuel cells such as proton exchange membrane fuel cells (PEMFC: Polymer Electrolyte Fuel Cell) and solid oxide fuel cells (SOFC: Solid Oxide Fuel Cell), hydrogen internal combustion engines, or hydrogen turbines.

[0010] When the green electricity generation system of the present invention actually generates green electricity, the hydrogen oxide production catalyst generated by the green hydrogen generation system of the present invention is transported to the lightning plasma decomposition unit 5 via the raw material transport pipe, where it is newly activated, deoxidized, and reduced to generate a hydrogen production catalyst. The hydrogen production catalyst produced by reduction is transported to the second hydrolysis reaction unit 6 through a raw material transport pipe, and undergoes a hydrolysis reaction with water transported to the second hydrolysis reaction unit 6 from an external water source through a water supply pipe to produce hydrogen and a hydrogen oxide production catalyst. At the same time, a large amount of heat of enthalpy is released when the hydrogen oxide production catalyst is produced. The heat content is transferred via the heat transfer tube to the second heat exchange module 51 installed in the lightning plasma decomposition unit 5 for absorption, and some of the reduction heat is used in the lightning plasma decomposition unit 5, reducing power consumption and improving the reduction decomposition efficiency of the hydrogen oxide production catalyst. The hydrogen oxide production catalyst produced in the second hydrolysis reaction unit 6 returns to the lightning plasma decomposition unit 5 via the raw material transport tube and can be repeatedly circulated between the lightning plasma decomposition unit 5 and the second hydrolysis reaction unit 6. The lightning plasma decomposition unit 5 reduces the hydrogen oxide production catalyst to produce a hydrogen production catalyst and also produces oxygen, which is transported to the hydrogen energy power generation unit 7 via a raw material transport pipe. The hydrogen produced by the second hydrolysis reaction unit 6 is transported to the hydrogen energy power generation unit 7 via a raw material transport pipe, and together with the oxygen transported to the hydrogen energy power generation unit 7, green electricity and water are produced. The water produced by the hydrogen energy power generation unit 7 is sent to the second hydrolysis reaction unit 6 via a water supply pipe, and supplies the water required when the second hydrolysis reaction unit 6 performs hydrolysis. The generated green electricity supplies the electricity required to operate the system, and may also be output to the outside of the system for use in various applications. The hydrogen oxide producing catalyst is any one of a common metal, a metal alloy, a metal oxide, and a combination thereof. Metals preferably include copper, iron, aluminum, tin, lead, zinc, sodium, calcium, lithium, potassium, nickel, magnesium, gallium, cadmium, silicon, titanium, and the like. Furthermore, the metal oxide preferably includes copper peroxide (CuO2), iron trioxide (Fe2O3), iron tetroxide (Fe3O4), aluminum oxide (Al2O3), tin dioxide (SnO2), lead dioxide (PbO2), zinc oxide (ZnO), sodium oxide (Na2O), calcium oxide (CaO), lithium oxide (Li2O), potassium oxide (K2O), nickel oxide (Ni2O), magnesium oxide (MgO), gallium oxide (Ga2O3), cadmium oxide (CdO), silicon dioxide (SiO2), titanium dioxide (TiO2), and the like.

[0011] Please refer to Fig. 3. As shown in Fig. 3, the green hydrogen and green electricity generation system of the present invention is integrally configured with a green hydrogen generation system and a green electricity generation system, and includes a raw material mixing unit 1. The raw material mixing unit 1 is connected to a raw material transport pipe of the external hydrogen production catalyst, the raw material mixing unit 1 and the first hydrolysis reaction unit 2 are connected to each other via a raw material transport pipe, and the first hydrolysis reaction unit 2 and the heat recovery unit 3 are connected to each other via a raw material transport pipe. The first hydrolysis reaction unit 2 has a first heat exchange module 21. The first heat exchange module 21 and the heat recovery unit 3 are connected to each other via a heat transfer pipe. The green hydrogen and green electricity generation system of the present invention further comprises a separation unit 4. The heat recovery unit 3 is connected to the separation unit 4 through a raw material transport pipe. The green hydrogen and green electricity generating system of the present invention further comprises an electric light plasma decomposition unit 5. The lightning plasma decomposition unit 5 is connected to the separation unit 4 via a raw material transport pipe. The lightning plasma decomposition unit 5 and the second hydrolysis reaction unit 6 are connected to each other via a raw material transport pipe. The lightning plasma decomposition unit 5 comprises a second heat exchange module 51 . The second heat exchange module 51 and the second hydrolysis reaction unit 6 are connected to each other via a heat transfer tube. The second hydrolysis reaction unit 6 and the heat recovery unit 3 are connected to each other via a raw material transport pipe. The green hydrogen and green electricity generation system of the present invention further comprises a hydrogen energy power generation unit 7 . The hydrogen energy power generation unit 7 is connected to the lightning plasma decomposition unit 5, the first hydrolysis reaction unit 2 and the second hydrolysis reaction unit 6 via raw material transport pipes. The hydrogen energy power generation unit 7 and the second hydrolysis reaction unit 6 are connected to each other via a water pipe. The raw material mixing unit 1 and the heat recovery unit 3 are each connected to a water pipe connected to an external water source.

[0012] When the green hydrogen and green electricity generating system of the present invention is actually used, the external hydrogen production catalyst is transported into the raw material mixing unit 1 through the raw material transport pipe. An external water source supplies water to be transported to the raw material mixing unit 1 via a water supply pipe. The hydrogen production catalyst and water are uniformly mixed within the raw material mixing unit 1. The mixture of the hydrogen production catalyst and water is transported via a raw material transport pipe to the first hydrolysis reaction unit 2. The mixture of the hydrogen production catalyst and water undergoes a hydrolysis reaction in the first hydrolysis reaction unit 2 to produce hydrogen and a hydrogen oxide production catalyst. A large amount of heat is released when the hydrogen oxide production catalyst is produced, along with some of the hydrogen production catalyst that has not yet completely reacted. The heat is absorbed by the first heat exchange module 21 installed in the first hydrolysis reaction unit 2 and transmitted to the heat recovery unit 3 via a heat transfer tube. The hydrogen production catalyst that has not yet completely reacted in the first hydrolysis reaction unit 2 is transported to the heat recovery unit 3 via a raw material transport pipe. An external water source supplies water which is transported to the heat recovery unit 3 via a water supply pipe, and the collected heat content and water excite the unreacted hydrogen production catalyst to react completely, producing hydrogen and hydrogen oxide production catalyst. The hydrogen and hydrogen oxide production catalyst produced by the heat recovery unit 3 and the first hydrolysis reaction unit 2 are transported to the separation unit 4 via a raw material transport pipe, where they are separated into gaseous green hydrogen and solid hydrogen oxide production catalyst. The green hydrogen may be provided for use within the system or may be output outside the system for use in various applications. The hydrogen oxide production catalyst is transported to the lightning plasma decomposition unit 5 through the raw material transport pipe, where it is newly activated, deoxidized and reduced to produce a hydrogen production catalyst. The hydrogen production catalyst produced by reduction is transported to the second hydrolysis reaction unit 6 through a raw material transport pipe and hydrolyzed to produce hydrogen and a hydrogen oxide production catalyst, while releasing a large amount of heat of enthalpy that is generated when the hydrogen oxide production catalyst is produced. The heat content is transferred through the heat transfer tube to the second heat exchange module 51 installed in the lightning plasma decomposition unit 5 and absorbed therein. Part of the reduction heat is used in the lightning plasma decomposition unit 5, reducing power consumption and increasing the reduction decomposition efficiency of the hydrogen oxide production catalyst. The hydrogen oxide production catalyst produced in the second hydrolysis reaction unit 6 is transported to the heat recovery unit 3 through the raw material transport pipe and can be cycled repeatedly between the heat recovery unit 3, separation unit 4, lightning plasma decomposition unit 5 and second hydrolysis reaction unit 6 in sequence. The lightning plasma decomposition unit 5 reduces the hydrogen oxide production catalyst to produce a hydrogen production catalyst and also produces oxygen, which is transported to the hydrogen energy power generation unit 7 via a raw material transport pipe. The hydrogen produced in the first hydrolysis reaction unit 2 and the second hydrolysis reaction unit 6 is transported to the hydrogen energy power generation unit via a raw material transport pipe, and together with the oxygen transported to the hydrogen energy power generation unit 7, green electricity and water are produced. The water produced by the hydrogen energy power generation unit 7 is sent to the second hydrolysis reaction unit 6 via a water supply pipe, and supplies the second hydrolysis reaction unit 6 with water necessary for hydrolysis. The green electricity generated by the hydrogen energy power generation unit 7 supplies the electricity required to operate the system, and may be output to the outside of the system for use in various applications.

[0013] The present invention enables the system to be self-sufficient in both green hydrogen and green electricity used in the system while the system is operating, and allows for continuous circulation. In addition, green hydrogen can be produced without using water electrolysis, and there is no need to use renewable electricity such as solar energy or wind power, which effectively reduces the costs of purchasing green hydrogen and green electricity. Furthermore, the present invention allows raw materials such as the hydrogen production catalyst and water that need to be used in the system to be continuously recycled by activating them again in the system even after the hydrogen production catalyst has been used. Additionally, water can be recovered and reused during the system's operation, significantly reducing the amount of external water required. Thus, the present invention can provide inexpensive green hydrogen and green electricity, effectively replacing fossil fuels and effectively resolving the problems of global climate change and global warming. Furthermore, the present invention has advantages such as reversibility and interchangeability in the generation of green hydrogen and green electricity. Therefore, green hydrogen can be generated and stored at night when electricity prices are low, and then used to generate green electricity during peak daytime hours. This flexibility and ability to implement in a variety of ways can increase revenue and enhance economic returns. The system of the present invention can also produce green hydrogen by adding water as hydrogen is used, depending on the amount needed on-site and on-demand. In this way, green hydrogen is produced using a solid hydrogen production catalyst, which can effectively solve problems such as danger and high costs involved in storing and transporting hydrogen.

[0014] Here, the lightning plasma decomposition unit 5 of the present invention may have a second heat exchange module 51 attached to the outside of the unit body 52 as shown in FIG. Within the unit body 52, an artificial lightning module 53, a lightning plasma decomposition module 54, an energy storage and readjustment module 55, and a separation and purification module 56 are sequentially installed. After entering the lightning plasma decomposition unit 5, the hydrogen oxide production catalyst undergoes artificial lightning treatment, lightning plasma decomposition treatment, energy storage readjustment treatment and separation and purification treatment in sequence, thereby reducing the hydrogen oxide production catalyst to produce a hydrogen production catalyst. Here, by using the lightning plasma decomposition unit 5, the hydrogen oxide production catalyst can be newly activated, deoxidized, and then reduced to generate a new hydrogen production catalyst that can be reused.

[0015] As can be seen from the above, the green hydrogen generation system, green electricity generation system, and method for implementing the green hydrogen and green electricity generation system of the present invention have the following advantages (1) to (6). (1) The present invention enables the system to be self-sufficient in both green hydrogen and green electricity while the system is in operation, and to continuously circulate these resources. In addition, green hydrogen can be produced without using water electrolysis, and there is no need to use renewable electricity such as solar energy or wind power, which effectively reduces the costs of purchasing green hydrogen and green electricity. (2) The present invention enables raw materials such as the hydrogen production catalyst and water that need to be used in the system to be continuously recycled by activating them again in the system even after the hydrogen production catalyst has been used. In addition, water is recovered and reused during the system's operation, significantly reducing the amount of external water required and saving costs. (3) The present invention allows raw materials such as hydrogen production catalysts and water that need to be used in the system to be recovered and reused during the system operation process, thereby producing inexpensive green hydrogen and green electricity.The production cost of this green hydrogen is cheaper than that of conventional technology, making it highly industrially competitive. (4) The system of the present invention can generate green hydrogen by adding water as hydrogen is used, according to on-site and on-demand requirements. In this way, green hydrogen is produced using a solid hydrogen production catalyst, which can effectively solve problems such as the difficulty and high cost of storing and transporting hydrogen. (5) The system of the present invention can provide inexpensive green hydrogen and green electricity, effectively replacing fossil fuels and effectively resolving the problems of global climate change and global warming. This will increase income and boost economic returns. (6) Because the system of the present invention provides green hydrogen and green electricity with features such as reversibility and interchangeability, it is possible to generate green hydrogen during times when electricity rates are low and green electricity during times when electricity rates are high. This flexibility in implementing various methods results in high economic returns. [Explanation of symbols]

[0016] 1 Raw material mixing unit 2. First hydrolysis reaction unit 3 Heat Recovery Unit 4 Separation Unit 5 Lightning Plasma Decomposition Unit 6 Second hydrolysis reaction unit 7 Hydrogen Energy Power Generation Unit 21 First heat exchange module 51 Second heat exchange module 52 Unit body 53 Artificial Lightning Module 54 Lightning Plasma Decomposition Module 55 Energy Reserve Reconditioning Module 56 Separation and purification module

Claims

1. 1. A method for implementing a green hydrogen production system, comprising: The green hydrogen generation system includes a raw material mixing unit and a separation unit, the raw material mixing unit is connected to a raw material transport pipe of an external hydrogen production catalyst, the raw material mixing unit is connected to a first hydrolysis reaction unit via a raw material transport pipe, the first hydrolysis reaction unit is connected to a heat recovery unit via a raw material transport pipe, the first hydrolysis reaction unit has a first heat exchange module, and the first heat exchange module is connected to the heat recovery unit via a heat transfer pipe; the separation unit is connected to the heat recovery unit and the first hydrolysis reaction unit via a raw material transport pipe, the raw material mixing unit and the heat recovery unit are each connected to a water pipe connected to an external water source; The hydrogen production catalyst is any one of common metals (also referred to as base metals), metal alloys, metal oxides, and combinations thereof; the externally mounted hydrogen production catalyst is transported into the raw material mixing unit through a raw material transport pipe; an external water source supplies water to be transported to the raw material mixing unit via a water pipe; a hydrogen production catalyst and water are mixed in the raw material mixing unit; a mixture of a hydrogen production catalyst and water is transported to the first hydrolysis reaction unit through a raw material transport pipe; a mixture of a hydrogen production catalyst and water undergoes a water decomposition reaction in the first hydrolysis reaction unit; While producing hydrogen and a hydrogen oxide production catalyst, a large amount of heat generated when the hydrogen oxide production catalyst is produced and a portion of the hydrogen production catalyst that has not yet reacted is released. The heat content is absorbed by the first heat exchange module provided in the first hydrolysis reaction unit; transported to the heat recovery unit via a heat transfer tube; the hydrogen production catalyst that has not yet reacted in the first hydrolysis reaction unit is transported to the heat recovery unit through a raw material transport pipe; an external water source supplies water that is transported to the heat recovery unit via a water pipe; The collected heat content and water excite the unreacted hydrogen production catalyst to react and produce hydrogen and hydrogen oxide production catalyst; the hydrogen and the hydrogen oxide production catalyst produced in the heat recovery unit and the first hydrolysis reaction unit are transported to the separation unit via a raw material transport pipe; The separation unit separates the green hydrogen into gaseous hydrogen and a solid hydrogen oxide production catalyst. How to implement a green hydrogen generation system.

2. A method for implementing a green hydrogen generation system as described in claim 1, characterized in that the metals include copper, iron, aluminum, tin, lead, zinc, sodium, calcium, lithium, potassium, nickel, magnesium, gallium, cadmium, silicon, and titanium, and the metal oxides include copper peroxide (CuO2), iron trioxide (Fe2O3), iron tetroxide (Fe3O4), aluminum oxide (Al2O3), tin dioxide (SnO2), lead dioxide (PbO2), zinc oxide (ZnO), sodium oxide (Na2O), calcium oxide (CaO), lithium oxide (Li2O), potassium oxide (K2O), nickel oxide (Ni2O), magnesium oxide (MgO), gallium oxide (Ga2O3), cadmium oxide (CdO), silicon dioxide (SiO2), and titanium dioxide (TiO2).

Images