Bionic hydrogen production and storage energy operation system
Through the bionic hydrogen storage energy operation system, the problem of electrolytic cells in the low proportion of fluctuating green electricity and high energy consumption of gaseous hydrogen storage is solved, and efficient and safe hydrogen storage management is achieved, which is suitable for urban hydrogen storage scenarios.
Patent Information
- Application Number
- CN202510795332.1
- Authority / Receiving Office
- CN · China
- Patent Type
- Applications(China)
- Current Assignee / Owner
- Filing Date
- 2025-06-15
- Publication Date
- 2025-09-05
AI Technical Summary
In the prior art, in the commercialization path of electrolytic cells to absorb fluctuating green electricity, the rated power of electrolytic cells is not high, and the gaseous hydrogen storage scheme has high energy consumption, large land area and high safety risks, resulting in high power abandonment rate and making it difficult to promote hydrogen energy storage in cities.
The bionic hydrogen storage energy operation system is adopted, including an integrated energy management system, energy output subsystem, hydrogen management subsystem and thermal management subsystem. By efficiently allocating power resources, combining solid hydrogen storage technology and air-cooling/heating technology, the operation of electrolytic cells and hydrogen storage modules is optimized to achieve efficient utilization and safe management.
The proportion of electrolytic cells in fluctuating green electricity is increased, energy consumption and footprint are reduced, system safety and energy utilization efficiency are improved, and high-frequency utilization of hydrogen is achieved.
Smart Images
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Abstract
Description
Technical Field
[0001] The present invention relates to the technical field of urban hydrogen energy storage, and discloses a bionic hydrogen production and storage energy operation system. Background Art
[0002] As a clean energy source for the 21st century, hydrogen energy involves many links in the industry, including hydrogen production, storage, and use. The use of electrolyzers to continuously produce hydrogen from fluctuating green electricity is a promising technology. This is because hydrogen has a very high mass energy (144Mj), is extremely easy to diffuse (2g / mol), and has a wide explosion limit (4%-75%). This makes solid-state hydrogen storage more suitable for urban hydrogen energy storage together with electrolyzers compared to gaseous hydrogen storage, organic hydrogen storage, and low-temperature liquid hydrogen storage.
[0003] Currently, the commercialization path for electrolyzers to absorb fluctuating green electricity primarily relies on green electricity forecasting, rapid electrolyzer response, and supporting hydrogen storage units. The proportion of hydrogen production power to the fluctuating green electricity power rating is relatively low (20%-30%), resulting in a high rate of power curtailment. Hydrogen storage primarily utilizes a low-pressure spherical tank combined with a high-pressure storage tank, which carries high energy consumption, requires a large floor space, and poses significant safety risks. This hydrogen production and storage technology combination is unsuitable for urban hydrogen energy storage. Summary of the Invention
[0004] In view of this, the present invention provides a bionic hydrogen production and storage energy operation system to solve the problems in the future promotion of urban hydrogen energy storage, such as the low proportion of the rated power of the electrolyzer in the rated power of fluctuating green electricity, the high energy consumption of the supporting gaseous hydrogen storage solution, the large footprint and the high safety risks.
[0005] The present invention provides a bionic hydrogen production and storage energy operation system, which includes an integrated energy management system, an energy output subsystem, a hydrogen management subsystem, and a thermal management subsystem:
[0006] The integrated energy management system is used to receive the power sent by the fluctuating green power system after being processed by the input inverter, and distribute the energy to the energy output subsystem, hydrogen management subsystem, and thermal management subsystem according to the system's preset operation method:
[0007] The energy output subsystem receives electrical energy from the fuel cell module and outputs electricity to the power load / grid via the output-end inverter. At the same time, it outputs electricity to the input-end inverter to ensure the continuous operation of the bionic hydrogen production and storage energy operation system.
[0008] The hydrogen management subsystem receives electricity from the integrated energy management system and constructs a complete electricity-to-hydrogen and electricity-to-hydrogen-to-electricity process through the electrolyzer module, solid-state hydrogen storage module, voltage regulation module, and hydrogen load / fuel cell module.
[0009] The thermal management subsystem, including an external clean water source, a (wind) cooling module, and a fuel cell module, provides cooling / heating to the solid-state hydrogen storage module, achieving efficient thermal management of the solid-state hydrogen storage module;
[0010] The rated input power of the electrolyzer module shall not be less than 60% of the rated power of fluctuating green electricity, and the rated hydrogen storage capacity of the solid-state hydrogen storage module shall not be less than 6 times the rated hourly hydrogen production of the electrolyzer module.
[0011] Furthermore, the technical solution of the bionic hydrogen energy production and storage method is as follows:
[0012] Step S1: Self-check the rated power of the fluctuating green power system, the historical parameters of the green power daily power, the rated power of the electrolyzer module, the rated hydrogen storage capacity of the solid-state hydrogen storage module, the rated power generation power of the fuel cell module, the power of the energy output subsystem, and the power parameters of the thermal management subsystem, and then proceed to step S2;
[0013] Step S2: Input the energy policy, and calculate the most efficient hydrogen production energy plan and the most efficient power transmission energy plan according to the self-test data while ensuring the low operating power of the bionic hydrogen production and storage energy operation system, and then proceed to step S3;
[0014] Step S3: Continuously predict hydrogen load for three hours, one day, three days, one week, one month, and one season based on historical hydrogen consumption using a professional model, and scientifically allocate power to the electrolyzer module and the output inverter through the integrated energy management system, and then proceed to step S4;
[0015] Step S4: Based on the time-of-use electricity price policy, the extreme energy plan of step S2, and different hydrogen loads, predict the economic benefits of the fuel cell module through time-of-use power generation through surplus hydrogen while ensuring the continuous operation of the bionic hydrogen production and storage energy operation system, and then proceed to step S5;
[0016] Step S5: According to the results of the above steps S1 to S4, the system is continuously operated, and the system self-optimization is continuously performed based on the accumulated professional models, and the steps S2 to S4 are looped;
[0017] Step S6: monitor the performance of the electrolyzer module, solid-state hydrogen storage module, and fuel cell module respectively, and issue a prompt when the performance of the above modules drops to 80% of the rated performance.
[0018] Furthermore, the energy output subsystem also includes a fuel cell module, a power channel between the fuel cell module and the energy output subsystem, a power channel from the energy output subsystem to the input inverter and the output inverter, and a power channel from the integrated energy management system to the output inverter.
[0019] Furthermore, the hydrogen management subsystem also includes a hydrogen production power supply in front of the electrolyzer module, a purification device behind the electrolyzer module, a mass flow meter, a pressure sensor, a one-way valve, and a switch valve between the electrolyzer module and the solid-state hydrogen storage module, a one-way valve and a switch valve between the solid-state hydrogen storage module and the pressure regulating module, a mass flow meter, a pressure reducing valve, and a switch valve between the pressure regulating module and the fuel cell module, and a mass flow meter, a pressure reducing valve, and a switch valve between the pressure regulating module and the hydrogen load. The switch valve can be manual or electromagnetic.
[0020] Furthermore, the electrolyzer module can be a PEM / AEM electrolyzer or other room-temperature water electrolysis hydrogen production equipment, and no boosting device is provided between the electrolyzer module and the solid-state hydrogen storage module.
[0021] Furthermore, the hydrogen load includes a fixed hydrogen load and a portable hydrogen load, the pressure of the hydrogen load is not higher than 1.6 MPa, and the hydrogen load is controlled from the hydrogen load to the pressure regulating module by a switch valve, which can be manual or electromagnetic.
[0022] Furthermore, the thermal management subsystem includes an external clean water bath and a (wind) heat dissipation module. The external clean water source is connected to the electrolyzer module to provide hydrogen production water to the electrolyzer, and is connected to the atomizer in the solid-state hydrogen storage module to provide a heat dissipation medium to the solid-state hydrogen storage module. The (wind) heat dissipation module provides forced convection wind to the solid-state hydrogen storage module. Under the evaporation of the heat dissipation medium, the solid-state hydrogen storage module is continuously cooled and absorbs hydrogen, providing forced convection wind to assist heat dissipation for the fuel cell module.
[0023] Furthermore, the heat supply scheme of the thermal management subsystem to maintain the continuous hydrogen release of the solid-state hydrogen storage module is as follows:
[0024] The forced ventilation heat source supplement scheme is to set up multiple groups of solid-state hydrogen storage modules. When the room temperature is higher than 20°C, the atomizer is turned off during the hydrogen release process, and forced ventilation is used to introduce external air to absorb the cold energy of the hydrogen storage module and remove it, thereby maintaining a stable hydrogen absorption state.
[0025] The auxiliary heating supplementary heat source solution can provide auxiliary warm air heating by connecting to a heat source / heat pump / other waste heat when the normal temperature is below 20°C or the hydrogen storage capacity of the solid-state hydrogen storage module is not high.
[0026] Furthermore, the bionic hydrogen production and storage energy operation system also includes a safety alarm system consisting of a hydrogen sensor, an alarm, and a flame detector, as well as an auxiliary emergency fire-fighting function composed of an external clean water source and a (wind) heat dissipation module in the thermal management subsystem.
[0027] Furthermore, the bionic hydrogen production and storage energy operation system also provides the application of bionic hydrogen production and storage operation in any urban hydrogen energy storage scenario.
[0028] The above technical solution of the present invention has at least the following beneficial effects:
[0029] The present invention provides a bionic hydrogen production and storage energy operation system, which uses a simulation operation method in combination with national energy policies to achieve high-value energy utilization, and uses the operating system's own hydrogen load in combination with a high-proportion fluctuating green electricity hydrogen production method to achieve high-frequency hydrogen utilization. It uses solid-state hydrogen storage technology to reduce the hydrogen boosting process, and uses air cooling / heating technology to improve energy efficiency, improve space utilization efficiency, and improve system safety. BRIEF DESCRIPTION OF THE DRAWINGS
[0030] In order to more clearly illustrate the specific embodiments of the present invention, the specific embodiments will be briefly introduced in conjunction with the drawings. Obviously, the drawings described below are some embodiments of the present invention. For ordinary technicians in this field, other drawings can be obtained based on these drawings without paying any creative work.
[0031] Figure 1 A structural schematic diagram of a bionic hydrogen production and storage energy operation system provided in an embodiment of the present invention. Figure 2 A flow chart of an operating method of a bionic hydrogen production and storage energy operating system provided in an embodiment of the present invention.
[0032] Description of reference numerals:
[0033] 1. Fluctuating green electricity system; 2. Integrated energy management system; 210. Energy output subsystem; 211. Input inverter; 212. Output inverter; 213. Power load; 220. Hydrogen management subsystem; 221. Electrolyzer module; 222. Solid-state hydrogen storage module; 223. Voltage regulation module; 224. Fuel cell module; 225. Hydrogen load; 230. Thermal management subsystem; 231. External clean water source; 232. (Wind) cooling module. DETAILED DESCRIPTION
[0034] The following examples are provided for a better understanding of the present invention, and are not intended to limit the best mode of implementation, nor to limit the content and scope of protection of the present invention. Any product identical or similar to the present invention obtained by anyone based on the inspiration of the present invention or combining the features of the present invention with other prior arts shall fall within the scope of protection of the present invention.
[0035] If the specific implementation steps or conditions are not specified in the examples, the procedures or conditions of the conventional experimental steps disclosed in the literature in this field can be followed. If the manufacturers of the reagents or instruments are not specified, they are all conventional reagents or products that can be purchased commercially.
[0036] The present invention is further described in detail below with reference to specific examples. These examples should not be construed as limiting the scope of protection claimed in the present invention.
[0037] Figure 1 A schematic diagram of a bionic hydrogen production and storage energy operation system provided by an embodiment of the present invention is shown in FIG. Figure 1 As shown, a bionic hydrogen production and storage energy operation system provided by an embodiment of the present invention includes an integrated energy management system 2, an energy output subsystem 210, a hydrogen management subsystem 220, and a thermal management subsystem 230:
[0038] The integrated energy management system 2 is used to receive the power sent by the fluctuating green power system 1 and processed by the input inverter 211, and distribute the energy to the energy output subsystem 210, the hydrogen management subsystem 220, and the thermal management subsystem 230 according to the system's preset operating method:
[0039] The energy output subsystem 210 receives power from the fuel cell module 224 and outputs power to the power load 213 / grid via the output inverter 212. It also outputs power to the input inverter 211, ensuring the continuous operation of the bionic hydrogen production and storage energy operation system.
[0040] The hydrogen management subsystem 220 is used to receive electricity distributed by the integrated energy management system 2 and build a complete electricity-to-hydrogen and electricity-to-hydrogen-to-electricity process through the electrolyzer module 221, solid-state hydrogen storage module 222, voltage regulation module 223, hydrogen load 225 / fuel cell module 224;
[0041] The thermal management subsystem 230 includes an external clean water source 231, a (wind) heat dissipation module 232, and a fuel cell module 224. It provides cooling / heating to the solid-state hydrogen storage module 222, thereby achieving efficient thermal management of the solid-state hydrogen storage module 222.
[0042] The rated input power of the electrolyzer module 221 shall not be less than 60% of the rated power of the fluctuating green electricity 1, and the rated hydrogen storage capacity of the solid-state hydrogen storage module 222 shall not be less than 6 times the rated hourly hydrogen production capacity of the electrolyzer module 221.
[0043] Furthermore, the technical solution of the bionic hydrogen energy production and storage method is as follows:
[0044] Step S1: Self-check the rated power of the fluctuating green power system 1, the historical parameters of the green power daily power, the rated power of the electrolyzer module 221, the rated hydrogen storage capacity of the solid-state hydrogen storage module 222, the rated power generation power of the fuel cell module 224, the power of the energy output subsystem 210, and the power parameters of the thermal management subsystem 230, and then proceed to step S2;
[0045] Step S2: Input the energy policy, and calculate the most efficient hydrogen production energy plan and the most efficient power transmission energy plan according to the self-test data while ensuring the low operating power of the bionic hydrogen production and storage energy operation system, and then proceed to step S3;
[0046] Step S3: Continuously predict hydrogen load for three hours, one day, three days, one week, one month, and one season based on historical hydrogen consumption using a professional model, and scientifically distribute power to the electrolyzer module 221 and the output inverter 212 through the integrated energy management system 2, and then proceed to step S4;
[0047] Step S4: Based on the time-of-use electricity price policy, the extreme energy plan of step S2, and different hydrogen loads, predict the economic benefits that the fuel cell module 224 can obtain through time-of-use power generation through surplus hydrogen while ensuring the continuous operation of the bionic hydrogen production and storage energy operation system, and then proceed to step S5;
[0048] Step S5: According to the results of the above steps S1 to S4, the system is continuously operated, and the system self-optimization is continuously performed based on the accumulated professional models, and the steps S2 to S4 are looped;
[0049] Step S6: monitor the performance of the electrolyzer module 221, the solid-state hydrogen storage module 222, and the fuel cell module 224 respectively, and issue a prompt when the performance of the above modules drops to 80% of the rated performance.
[0050] Furthermore, the energy output subsystem 210 also includes a fuel cell module 224, a power channel between the fuel cell module 224 and the energy output subsystem 210, a power channel from the energy output subsystem 210 to the input end inverter 211 and the output end inverter 212, and a power channel from the integrated energy management system 2 to the output end inverter 213.
[0051] Furthermore, the hydrogen management subsystem 220 also includes a hydrogen production power supply in front of the electrolyzer module 221, a purification equipment behind the electrolyzer module 221, a mass flow meter, a pressure sensor, a one-way valve, and a switch valve between the electrolyzer module 221 and the solid-state hydrogen storage module 222, a one-way valve and a switch valve between the solid-state hydrogen storage module 222 and the pressure regulating module 223, a mass flow meter, a pressure reducing valve, and a switch valve between the pressure regulating module 223 and the fuel cell module 224, and a mass flow meter, a pressure reducing valve, and a switch valve between the pressure regulating module 223 and the hydrogen load 225. The switch valve can be manual or electromagnetic.
[0052] Furthermore, the electrolyzer module 221 may be a PEM / AEM electrolyzer or other room-temperature water electrolysis hydrogen production equipment, and no boosting device is provided between the electrolyzer module 221 and the solid-state hydrogen storage module 222 .
[0053] Furthermore, the hydrogen load 225 includes a fixed hydrogen load and a portable hydrogen load, and the pressure of the hydrogen load is not higher than 1.6 MPa. The hydrogen load 225 and the pressure regulating module 223 are controlled by a switch valve, which can be manual or electromagnetic.
[0054] Furthermore, the thermal management subsystem 230 includes an external clean water source 231 and a (wind) heat dissipation module 232. The external clean water source 231 is connected to the electrolyzer module 221 to provide a hydrogen production water source to the electrolyzer module, and is connected to the atomizer in the solid-state hydrogen storage module 222 to provide a heat dissipation medium to the solid-state hydrogen storage module 222. The (wind) heat dissipation module 232 provides forced convection wind to the solid-state hydrogen storage module 222. Under the evaporation action of the heat dissipation medium, the solid-state hydrogen storage module 222 is continuously cooled and absorbs hydrogen, providing forced convection wind to assist heat dissipation for the fuel cell module 224.
[0055] Furthermore, the heat supply scheme of the thermal management subsystem 230 to maintain the solid-state hydrogen storage module 2220 to continuously release hydrogen is as follows:
[0056] The forced ventilation heat source supplement scheme is to set up multiple groups of solid hydrogen storage modules 222. When the room temperature is higher than 20°C, the atomizer is turned off during the hydrogen release process, and forced ventilation is used to introduce external air to absorb the cold energy of the hydrogen storage module and remove it, thereby maintaining a stable hydrogen absorption state.
[0057] The auxiliary heating supplementary heat source solution can perform auxiliary warm air heating by connecting to a heat source / heat pump / other waste heat when the normal temperature is lower than 20°C or the hydrogen storage capacity of the solid-state hydrogen storage module 222 is not high.
[0058] Furthermore, the bionic hydrogen production and storage energy operation system also includes a safety alarm system consisting of a hydrogen sensor, an alarm, and a flame detector, as well as an auxiliary emergency fire-fighting function composed of an external clean water source 231 and a (wind) heat dissipation module 232 in the thermal management subsystem 230.
[0059] Furthermore, the bionic hydrogen production and storage energy operation system also provides the application of bionic hydrogen production and storage operation in any urban hydrogen energy storage scenario.
[0060] A bionic hydrogen production and storage energy operation system of the present invention is mainly arranged around the hydrogen load 205 in non-chemical parks in urban areas, combined with the fluctuating green electricity system 1 in the region, and uses a simulation operation method combined with national energy policies to achieve high-value energy utilization. The hydrogen load of the operation system itself is combined with a high-proportion fluctuating green electricity hydrogen production method to achieve high-frequency utilization of hydrogen. Solid-state hydrogen storage technology is used to reduce the hydrogen boosting process, and air cooling / heating technology is used to improve energy efficiency, improve space utilization efficiency, and improve system safety.
[0061] Obviously, the above embodiments are merely examples for clarity of explanation and are not intended to limit the implementation methods. Those skilled in the art will readily appreciate that other variations or modifications based on the above descriptions are possible. It is not necessary and impossible to enumerate all implementation methods here. Obvious variations or modifications arising therefrom remain within the scope of protection of the present invention.
Claims
1. A bionic hydrogen production and storage energy operation system, characterized in that: The bionic hydrogen production and storage energy operation system includes an integrated energy management system, an energy output subsystem, a hydrogen management subsystem, and a thermal management subsystem; The integrated energy management system is used to receive the power sent by the fluctuating green power system after being processed by the input inverter, and distribute the energy to the energy output subsystem, hydrogen management subsystem, and thermal management subsystem according to the system bionic operation method: The energy output subsystem receives electrical energy from the fuel cell module and outputs electricity to the power load / grid via the output-end inverter. At the same time, it outputs electricity to the input-end inverter to ensure the continuous operation of the bionic hydrogen production and storage energy operation system. The hydrogen management subsystem receives electricity from the integrated energy management system and constructs a complete electricity-to-hydrogen and electricity-to-hydrogen-to-electricity process through the electrolyzer module, solid-state hydrogen storage module, voltage regulation module, and hydrogen load / fuel cell module. The thermal management subsystem, including an external clean water source, a (wind) cooling module, and a fuel cell module, provides cooling / heating to the solid-state hydrogen storage module, achieving efficient thermal management of the solid-state hydrogen storage module; The rated input power of the electrolyzer module shall not be less than 60% of the rated power of fluctuating green electricity, and the rated hydrogen storage capacity of the solid-state hydrogen storage module shall not be less than 6 times the rated hourly hydrogen production of the electrolyzer module.
2. A bionic hydrogen production and storage energy operation system according to claim 1, characterized in that: The integrated energy management system operates as follows: Step S1: Self-check the rated power of the fluctuating green power system, the historical parameters of the green power daily power, the rated power of the electrolyzer module, the rated hydrogen storage capacity of the solid-state hydrogen storage module, the rated power generation power of the fuel cell module, the power of the energy output subsystem, and the power parameters of the thermal management subsystem, and then proceed to step S2; Step S2: Input the energy policy, and calculate the most efficient hydrogen production energy plan and the most efficient power transmission energy plan according to the self-test data while ensuring the low operating power of the bionic hydrogen production and storage energy operation system, and then proceed to step S3; Step S3: Continuously predict hydrogen load for three hours, one day, three days, one week, one month, and one season based on historical hydrogen consumption using a professional model, and scientifically allocate power to the electrolyzer module and the output inverter through the integrated energy management system, and then proceed to step S4; Step S4: Based on the time-of-use electricity price policy, the extreme energy plan of step S2, and different hydrogen loads, predict the economic benefits of the fuel cell module through time-of-use power generation through surplus hydrogen while ensuring the continuous operation of the bionic hydrogen production and storage energy operation system, and then proceed to step S5; Step S5: According to the results of the above steps S1-S4, the system is continuously operated and self-optimized according to the accumulated professional models, and the loop of steps S2-S4 is entered; Step S6: monitor the performance of the electrolyzer module, solid-state hydrogen storage module, and fuel cell module respectively, and issue a prompt when the performance of the above modules drops to 80% of the rated performance.
3. The energy output subsystem according to claim 1, characterized in that: The energy output includes the fuel cell module, the power channel between the fuel cell module and the energy output subsystem, the power channel from the energy output subsystem to the input inverter and the output inverter, and the power channel from the integrated energy management system to the output inverter.
4. The hydrogen management subsystem according to claim 1, characterized in that: It also includes a hydrogen production power supply in front of the electrolyzer module, purification equipment behind the electrolyzer module, a mass flow meter, a pressure sensor, a one-way valve, and a switch valve between the electrolyzer module and the solid-state hydrogen storage module, a one-way valve and a switch valve between the solid-state hydrogen storage module and the pressure regulating module, a mass flow meter, a pressure reducing valve, and a switch valve between the pressure regulating module and the fuel cell module, and a mass flow meter, a pressure reducing valve, and a switch valve between the pressure regulating module and the hydrogen load. The switch valve can be manual or electromagnetic.
5. The electrolyzer module according to claim 4, characterized in that It can be a PEM / AEM electrolyzer or other room temperature water electrolysis hydrogen production equipment, and no booster device is provided between the electrolyzer module and the solid-state hydrogen storage module.
6. The hydrogen load according to claim 4, characterized in that: It also includes fixed hydrogen loads and portable hydrogen loads. The pressure of the hydrogen load is not higher than 1.6Mpa. The hydrogen load and the pressure regulating module are controlled by a switch valve, which can be manual or electromagnetic.
7. The thermal management subsystem according to claim 1, wherein: The thermal management subsystem includes an external clean water bath and a (wind) heat dissipation module. The external clean water source is connected to the electrolyzer module to provide hydrogen production water to the electrolyzer, and is connected to the atomizer in the solid-state hydrogen storage module to provide a heat dissipation medium to the solid-state hydrogen storage module. The (wind) heat dissipation module provides forced convection wind to the solid-state hydrogen storage module. Under the evaporation of the heat dissipation medium, the solid-state hydrogen storage module is continuously cooled and absorbs hydrogen, providing forced convection wind to assist heat dissipation for the fuel cell module.
8. The heat supply scheme for maintaining the continuous hydrogen release of the solid-state hydrogen storage module by the thermal management subsystem according to claim 7 can adopt the following scheme: Forced ventilation to supplement the heat source: multiple groups of solid-state hydrogen storage modules are set up. When the room temperature is higher than 20°C, the atomizer is turned off during the hydrogen release process, and forced ventilation is used to introduce external air to absorb the cold energy of the hydrogen storage module and bring it out to maintain a stable hydrogen absorption state; Auxiliary heating supplementary heat source: When the room temperature is lower than 20℃ or the hydrogen storage capacity of the solid-state hydrogen storage module is not high, auxiliary warm air heating can be performed by connecting to the heat source / heat pump / other waste heat in the working state of the fuel cell.
9. The bionic hydrogen production and storage energy operation system according to claim 1, characterized in that: The bionic hydrogen production and storage energy operation system also includes a safety alarm system consisting of a hydrogen sensor, an alarm, and a flame detector, as well as an auxiliary emergency fire-fighting function composed of an external clean water source and a (wind) heat dissipation module in the thermal management system.
10. A bionic hydrogen production and storage energy operation system, characterized in that: The bionic hydrogen production and storage energy operation system uses the application of bionic hydrogen production and storage energy operation in any urban hydrogen energy storage scenario of claims 1-9.