Hydrogen collaborative preparation method based on wind power

Abstract

The invention discloses a wind power-based hydrogen cooperative preparation method, which realizes the cooperation between power supply and hydrogen production of a power grid through the design of a cooperative hydrogen production device, and effectively converts the residual electric energy into the chemical energy of hydrogen under the condition of ensuring the power supply demand. The first electrolytic cell is surrounded by the second electrolytic cell, heat provided by the cooperative hydrogen production device for the second electrolytic cell can adjust the reaction condition of the second electrolytic cell and can also indirectly adjust the reaction condition for the first electrolytic cell, and electrolyte in the first electrolytic cell can also react in the second electrolytic cell through the heat capacity of the electrolyte. Heat preservation is provided so as to improve the energy conversion rate of residual electric energy. When the chemical reaction is in a stable state, the energy conversion efficiency is more stable than that in a non-stable state, and the efficiency of a downstream hydrogen precipitation process is improved, so that the overall working efficiency of the cooperative hydrogen production device is improved, and the overall energy consumption of the cooperative hydrogen production device is reduced.

Description

Technical Field

[0001] The present application relates to the field of fuel preparation technology, and in particular to a wind power-based coordinated hydrogen preparation method. Background Art

[0002] As a fuel, hydrogen has a wide range of application scenarios, and the preparation of hydrogen has also become one of the main development directions of fuel preparation technology. For example, the publication (announcement) number is CN104327902A, and the patent title is: "A device for desulfurizing and producing hydrogen by electrolyzing water-coal slurry" (main classification number: C10L9 / 02). The electrolyte used is recycled, saving time and resources, with mild reaction and convenient operation. For another example, the publication (announcement) number is CN110819418A, and the patent title is: "A method for efficient desulfurization and hydrogen production based on solar energy STEP thermal-electrochemical coupling" (main classification number: C10L9 / 02), which realizes the preparation of hydrogen based on solar energy. On the one hand, it can be shown that the preparation technology of hydrogen as a fuel has strong technical feasibility; on the other hand, it can also be shown that the technical mining in this field still has a relatively broad expansion prospect.

[0003] As a clean energy, the development and promotion of wind power technology has attracted much attention. At the same time, wind power also has certain disadvantages. For example, the unstable wind resources make its power generation unstable. This problem is usually solved by equipping wind turbines with energy storage devices. Energy storage devices can convert wind-based electrical energy into chemical energy for storage. Energy storage devices are such as hydrogen production devices.

[0004] However, in addition to the requirements for reaction current and reaction voltage, the preparation of hydrogen also has conditional requirements for reaction temperature. In order to achieve these conditions, there will be a certain consumption of electric energy. If the electricity that wind turbines can feed into the power grid is affected in order to meet the conditions for hydrogen production, it will affect the electricity consumption of enterprises and residents. How to effectively convert the remaining electricity into chemical energy such as hydrogen on the basis of meeting the electricity consumption of enterprises and residents to achieve the synergy between power supply and hydrogen production has become an urgent problem to be solved. Summary of the invention

[0005] The embodiments of the present application provide a wind power-based coordinated hydrogen production method to at least partially solve the above-mentioned technical problems.

[0006] The present application embodiment adopts the following technical solutions: In a first aspect, an embodiment of the present application provides a wind power-based coordinated hydrogen production method, the method is based on a coordinated hydrogen production device, the device includes a first electrolyzer and a second electrolyzer arranged on the outer peripheral side of the first electrolyzer, the first electrolyzer and the second electrolyzer are isolated from each other in internal space, so that there is no material exchange between the first electrolyzer and the second electrolyzer, but there is heat exchange, the method includes: Using the surplus electric energy generated by the wind turbine generator set and not fed into the power grid to heat the electrolyte in the second electrolytic cell; When the first condition is met, the electrodes in the second electrolytic cell are energized so that the current of the electrodes in the second electrolytic cell reaches the first current; the first condition includes one of the following: the duration of the wind turbine generator set being in a full-load state reaches a preset first duration, and the duration of the electrolyte heating in the second electrolytic cell reaches a preset second duration; the temperature of the electrolyte in the second electrolytic cell reaches a first reaction temperature, which is the reaction temperature of the second electrolytic cell that can achieve the highest efficiency and stable reaction under the condition of the first current; When the second condition is met, the current of the electrode in the second electrolytic cell is increased to the second current; the second condition includes one of the following: within a first time period after the first condition is met, the change in the instantaneous output power of the wind turbine generator set is less than a preset change threshold, and the oxygen content of the electrolyte in the second electrolytic cell reaches a preset oxygen content threshold; the temperature of the electrolyte in the second electrolytic cell reaches a second reaction temperature, and the second reaction temperature is the reaction temperature of the second electrolytic cell that can achieve the highest efficiency and stable reaction under the condition of the second current; If it is detected that the temperature of the electrolyte in the first electrolytic cell reaches the first reaction temperature, the electrodes in the first electrolytic cell are energized so that the current of the electrodes in the first electrolytic cell reaches the first current, so that the first electrolytic cell performs an electrolytic hydrogen production reaction.

[0007] In an optional embodiment of this specification, the method further includes: When the third condition is met, stop energizing the electrodes in the first electrolytic cell; the third condition includes: the duration for which the change in the instantaneous output power of the wind turbine generator set is greater than the change threshold is greater than a preset third duration; the third duration is negatively correlated with the maximum single-unit capacity of the wind turbine generator set, negatively correlated with the total capacity of the wind turbine generator set, and positively correlated with the volume of the second electrolytic cell.

[0008] In an optional embodiment of this specification, the method further includes: When a fourth condition is reached, powering the electrodes in the second electrolytic cell is stopped; the fourth condition includes: the temperature of the electrolyte in the first electrolytic cell is lower than the first reaction temperature.

[0009] In an optional embodiment of this specification, the method further includes: The cooperative hydrogen production device also includes a thermal insulation layer; the thermal insulation layer is arranged on the side of the second electrolytic cell facing the external environment.

[0010] In an optional embodiment of this specification, the method further includes: The first electrolytic cell and the second electrolytic cell are both electrolytic cells based on anion exchange membrane technology.

[0011] In an optional embodiment of this specification, the method further includes: The first reaction temperature is between 50 degrees Celsius and 70 degrees Celsius; The second reaction temperature is between 70 degrees Celsius and 90 degrees Celsius.

[0012] In an optional embodiment of this specification, the method further includes: The capacity of the first electrolytic tank is smaller than the capacity of the second electrolytic tank.

[0013] In an optional embodiment of this specification, the method further includes: According to the temperature of the electrolyte in the first electrolytic cell, plotting a temperature versus time curve; When the temperature change curve over time shows that the first electrolytic cell is in a heating state and the heating rate is greater than a preset rate threshold, the judgment of the first condition is performed; the rate threshold is negatively correlated with the difference in capacity between the first electrolytic cell and the second electrolytic cell.

[0014] In a second aspect, an embodiment of the present application further provides a wind power-based coordinated hydrogen production device, which is used to implement the method in the first aspect.

[0015] In a third aspect, an embodiment of the present application further provides an electronic device, including: Processor; and A memory arranged to store computer executable instructions which, when executed, cause the processor to perform the method steps described in the first aspect.

[0016] In a fourth aspect, an embodiment of the present application further provides a computer-readable storage medium, which stores one or more programs. When the one or more programs are executed by an electronic device including multiple applications, the electronic device executes the method steps described in the first aspect.

[0017] At least one of the above technical solutions adopted in the embodiments of the present application can achieve the following beneficial effects: The technical solution in the present application realizes the coordination between power supply for the power grid and hydrogen production through the design of the cooperative hydrogen production device, and ensures that the surplus electric energy is more effectively converted into the chemical energy of hydrogen while ensuring the power supply demand. The first electrolyzer is surrounded by the second electrolyzer. In addition to adjusting the reaction conditions of the second electrolyzer, the heat provided by the cooperative hydrogen production device to the second electrolyzer can also indirectly adjust the reaction conditions for the first electrolyzer, and the electrolyte in the first electrolyzer can also provide insulation for the reaction in the second electrolyzer through its heat capacity to improve the energy conversion rate of the surplus electric energy. When the chemical reaction is in a stable state, its energy conversion efficiency is more stable than that in a non-steady state, and it is also beneficial to the efficiency of the downstream hydrogen precipitation process, thereby improving the overall working efficiency of the cooperative hydrogen production device and reducing the overall energy consumption of the cooperative hydrogen production device. In the method in the present application, under certain conditions, the first electrolyzer can also carry out hydrogen production reaction. Although the hydrogen production efficiency may not be higher than that of the second electrolyzer, when the electrolyte temperature is appropriate, the surplus electric energy can also be converted into chemical energy, thereby improving the hydrogen production efficiency. BRIEF DESCRIPTION OF THE DRAWINGS

[0018] The drawings described herein are used to provide a further understanding of the present application and constitute a part of the present application. The illustrative embodiments of the present application and their descriptions are used to explain the present application and do not constitute an improper limitation on the present application. In the drawings: Figure 1 A schematic diagram of a process of a wind power-based hydrogen collaborative production method provided in an embodiment of this specification; Figure 2 It is a schematic diagram of the structure of an electronic device in an embodiment of this specification. DETAILED DESCRIPTION

[0019] The present invention is further described in detail below by specific embodiments in conjunction with the accompanying drawings. Wherein similar elements in different embodiments adopt associated similar element numbers. In the following embodiments, many detailed descriptions are for making the present application better understood. However, those skilled in the art can easily recognize that some features can be omitted in different situations, or can be replaced by other elements, materials, methods. In some cases, some operations related to the present application are not shown or described in the specification, and this is to avoid the core part of the present application being overwhelmed by too much description, and for those skilled in the art, it is not necessary to describe these related operations in detail, and they can fully understand the related operations according to the description in the specification and the general technical knowledge in the art.

[0020] In addition, the features, operations or characteristics described in the specification can be combined in any appropriate manner to form various implementations. At the same time, the steps or actions in the method description can also be interchanged or adjusted in a manner that is obvious to those skilled in the art. Therefore, the various sequences in the specification and the drawings are only for the purpose of clearly describing a certain embodiment and are not meant to be a required sequence, unless otherwise specified that a certain sequence must be followed.

[0021] The serial numbers of the components in this document, such as "first", "second", etc., are only used to distinguish the objects described and do not have any order or technical meaning. The "connection" and "coupling" mentioned in this application, unless otherwise specified, include direct and indirect connections (couplings).

[0022] The technical solutions provided by various embodiments of the present application are described in detail below in conjunction with the accompanying drawings.

[0023] like Figure 1 As shown, the wind power-based hydrogen synergistic production method in this specification includes the following steps: S100: using the surplus electric energy generated by the wind turbine generator set but not fed into the power grid to heat the electrolyte in the second electrolytic cell.

[0024] The method in this specification is based on a collaborative hydrogen production device, which includes a first electrolyzer and a second electrolyzer arranged on the outer peripheral side of the first electrolyzer. The internal spaces of the first electrolyzer and the second electrolyzer are isolated, so that there is no material exchange between the first electrolyzer and the second electrolyzer, but there is heat exchange, and the heat exchange can be in the form of thermal radiation. In an optional embodiment of the present specification, the collaborative hydrogen production device also includes a thermal insulation layer; the thermal insulation layer is arranged on the side of the second electrolyzer facing the external environment. In addition, the collaborative hydrogen production device in this specification may also include an electrode arranged in the first electrolyzer, an electrode arranged in the second electrolyzer, a downstream hydrogen evolution device, etc.

[0025] The surplus electric energy in this specification refers to the electric energy that cannot be connected to the power grid and cannot be consumed by other means. The cooperative hydrogen production device in this specification can be completely powered by wind turbines, so it is difficult to accurately estimate the amount of surplus electricity at different times. In other words, at different times, the cooperative hydrogen production device can provide different conditions for hydrogen production. When the surplus electricity is not enough to provide complete hydrogen production conditions, you can first choose to use the surplus electricity to heat the electrolyte in the second electrolyzer. As for whether the temperature of the heated electrolyte can reach the reaction temperature of the hydrogen production reaction, it depends on the amount of surplus electricity. The hydrogen production reaction in this specification is hydrogen production by electrolysis, so the electrolyte can be water, or other catalysts can be added.

[0026] Of course, in an online production environment, it is possible that all the electricity obtained by the wind turbine generator set is connected to the power grid and there is no surplus electricity, so there is no need to execute the method in this specification.

[0027] S102: When the first condition is met, energize the electrodes in the second electrolytic cell so that the current of the electrodes in the second electrolytic cell reaches a first current.

[0028] The electrolysis reaction cannot be carried out by simply heating the electrolyte; the electrolyte must also be energized.

[0029] The first condition in this specification includes one of the following: the duration of the wind turbine generator set being in a full-load state reaches a preset first duration, and the duration of the electrolyte heating in the second electrolyzer reaches a preset second duration (indicating that the wind turbine generator set is outputting electrical energy at a relatively large power for a certain period of time, the probability of an instantaneous decrease in output power is relatively small, and the remaining electrical energy is relatively sufficient, and the possibility of achieving hydrogen production is relatively large), wherein the first duration and the second duration can both be empirical values, which are related to the capacity of the wind turbine generator set; the temperature of the electrolyte in the second electrolyzer reaches the first reaction temperature (indicating that the reaction conditions have been met), and the first reaction temperature is the reaction temperature of the second electrolyzer that can achieve the highest efficiency under the condition of the first current when the reaction is stable (stable reaction is a reaction state in which the reaction rate changes less, which can be regarded as a constant reaction rate). The correspondence between the first current and the first reaction temperature can be obtained by experiment. In this specification, the first reaction temperature is a reaction temperature with a lower reaction rate. This correspondence is related to factors such as catalysts. In the case where the second electrolyzer is an electrolyzer based on anion exchange membrane technology, the first reaction temperature is between 50 degrees Celsius and 70 degrees Celsius. The hydrogen production process in this specification is intended to keep the reaction in a stable state, thereby ensuring energy conversion efficiency.

[0030] S104: When the second condition is met, increasing the current of the electrodes in the second electrolytic cell to a second current.

[0031] Due to the conditions of wind power generation, the surplus electric energy may be on an increasing trend, and the first reaction temperature may not be able to achieve the full conversion of the surplus electric energy, and the reaction needs to be adjusted smoothly.

[0032] The second condition in this specification includes one of the following: within a first time period after the first condition is met (the first time period may be an empirical value, which is related to the capacity of the wind turbine generator set and the historical demand for electric energy of the power grid), the change in the instantaneous output power of the wind turbine generator set is less than a preset change threshold, and the oxygen content of the electrolyte in the second electrolyzer reaches a preset oxygen content threshold (indicating that the output of the wind turbine generator is stable, and the electrolysis reaction in the second electrolyzer has reached the maximum reaction efficiency under the current reaction conditions, and there are conditions for improving the reaction efficiency. The change threshold may be an empirical value. The oxygen content threshold may be the saturated content of oxygen in the electrolyte under the current conditions); the temperature of the electrolyte in the second electrolyzer reaches a second reaction temperature, which is the reaction temperature of the second electrolyzer that can achieve the highest efficiency and stable reaction under the second current (the second reaction temperature is higher than the first reaction temperature. In order to meet the needs of the hydrogen production reaction, in addition to power supply from other aspects, the remaining electric energy is used to heat the second electrolyzer, that is, the temperature of the second electrolyzer also has the function of monitoring the amount of remaining electric energy. The temperature of the second electrolyzer reaches the second reaction stability, indicating that there is a lot of remaining electric energy and the reaction rate should be increased). The corresponding relationship between the second reaction temperature and the second current can also be obtained through experiments.

[0033] In an optional embodiment of the present specification, when the second electrolytic cell is an electrolytic cell based on anion exchange membrane technology, the second reaction temperature is between 70 degrees Celsius and 90 degrees Celsius.

[0034] S106: If it is detected that the temperature of the electrolyte in the first electrolytic cell reaches the first reaction temperature, energize the electrodes in the first electrolytic cell so that the current of the electrodes in the first electrolytic cell reaches the first current, so that the first electrolytic cell performs an electrolytic hydrogen production reaction.

[0035] Since the second electrolytic cell is arranged on the outer peripheral side of the first electrolytic cell, the second electrolytic cell can also serve to heat the first electrolytic cell. When the amount of residual electric energy is large and the reaction of the second electrolytic cell is not sufficient to completely convert it into chemical energy, the first electrolytic cell can also carry out hydrogen production reaction to improve the energy conversion efficiency.

[0036] When the output power of the wind turbine generator set is continuously high, the amount of residual electric energy may be large. At this time, the first electrolyzer has reached a stable reaction and should not be destroyed. In an optional embodiment of the present specification, when the first electrolyzer has been performing a hydrogen production reaction under the first current, the heating of the first electrolyzer is turned on (a heating device may be provided in the first electrolyzer), and the reaction in the first electrolyzer reaches a stable reaction corresponding to the second reaction temperature.

[0037] In an optional embodiment of the present specification, the first electrolytic cell is also an electrolytic cell based on anion exchange membrane technology, and the composition of the material in the first electrolytic cell can be the same as the composition of the material in the second electrolytic cell. In order to improve the first electrolytic cell's ability to switch from a stable reaction corresponding to the first reaction temperature to a stable reaction corresponding to the second reaction temperature more sensitively, and to avoid the second electrolytic cell heating the first electrolytic cell and causing the second electrolytic cell to heat too slowly, in an optional embodiment of the present specification, the capacity of the first electrolytic cell is less than the capacity of the second electrolytic cell. According to the temperature of the electrolyte in the first electrolytic cell, a temperature variation curve is drawn; when the temperature variation curve indicates that the first electrolytic cell is in a heating state, and the heating rate is greater than a preset rate threshold, the judgment of the first condition is performed; the rate threshold is negatively correlated with the difference in the capacity of the first electrolytic cell and the second electrolytic cell.

[0038] The technical solution in the present application realizes the coordination between power supply for the power grid and hydrogen production through the design of the cooperative hydrogen production device, and ensures that the surplus electric energy is more effectively converted into the chemical energy of hydrogen while ensuring the power supply demand. The first electrolyzer is surrounded by the second electrolyzer. In addition to adjusting the reaction conditions of the second electrolyzer, the heat provided by the cooperative hydrogen production device to the second electrolyzer can also indirectly adjust the reaction conditions for the first electrolyzer, and the electrolyte in the first electrolyzer can also provide insulation for the reaction in the second electrolyzer through its heat capacity to improve the energy conversion rate of the surplus electric energy. When the chemical reaction is in a stable state, its energy conversion efficiency is more stable than that in a non-steady state, and it is also beneficial to the efficiency of the downstream hydrogen precipitation process, thereby improving the overall working efficiency of the cooperative hydrogen production device and reducing the overall energy consumption of the cooperative hydrogen production device. In the method in the present application, under certain conditions, the first electrolyzer can also carry out hydrogen production reaction. Although the hydrogen production efficiency may not be higher than that of the second electrolyzer, when the electrolyte temperature is appropriate, the surplus electric energy can also be converted into chemical energy, thereby improving the hydrogen production efficiency.

[0039] The electric energy output by the wind turbine generator set may be in an increasing trend or in a decreasing trend. In the case where the electric energy output by the wind turbine generator set is in a decreasing trend, the remaining electric energy will also decrease. In an optional embodiment of the present specification, it is determined whether the third condition is met. If the third condition is met, stop energizing the electrodes in the first electrolyzer (if the heating device in the first electrolyzer is turned on, the heating device in the first electrolyzer also needs to be turned off); the third condition includes: the duration of the change in the instantaneous output power of the wind turbine generator set is greater than the change threshold, and is greater than a preset third duration (indicating that there is fluctuation, and the fluctuation is continuous, making it difficult to provide stable conditions for hydrogen production under current conditions); the third duration is negatively correlated with the maximum single-unit capacity of the wind turbine generator set (fluctuations are mostly caused by wind conditions, and the larger the single-unit capacity, the higher the possibility of increased fluctuations, resulting in more obvious fluctuations and easy to detect), negatively correlated with the total capacity of the wind turbine generator set, and positively correlated with the volume of the second electrolyzer (due to the large specific heat capacity of water, the larger the volume, the more obvious the delay caused by the impact of changes in reaction conditions, and there is no need to rush to adjust).

[0040] As the output power of the wind turbine generator set further decreases, the remaining electric energy will also further decrease. When the fourth condition is reached, stop energizing the electrodes in the second electrolytic cell; the fourth condition includes: the temperature of the electrolyte in the first electrolytic cell is lower than the first reaction temperature. In this specification, in addition to being able to keep the second electrolytic cell warm, the temperature of the first electrolytic cell also has the function of detecting the remaining electric energy. When the temperature of the first electrolytic cell is lower than the first reaction temperature, it indicates that the temperature of the second electrolytic cell has also dropped to near the first reaction temperature, or even below the first reaction temperature, and at this time the remaining electric energy is still on a downward trend. It is difficult to continue to power the electrodes and maintain the electrolysis reaction. Therefore, the electrolysis reaction in the second electrolytic cell is stopped.

[0041] Figure 2 This is a schematic diagram of the structure of an electronic device according to an embodiment of the present application. Figure 2 At the hardware level, the electronic device includes a processor, and optionally also includes an internal bus, a network interface, and a memory. The memory may include a memory, such as a high-speed random access memory (RAM), and may also include a non-volatile memory (non-volatile memory), such as at least one disk storage. Of course, the electronic device may also include hardware required for other services.

[0042] The processor, network interface and memory can be interconnected through an internal bus, which can be an ISA (Industry Standard Architecture) bus, a PCI (Peripheral Component Interconnect) bus or an EISA (Extended Industry Standard Architecture) bus. The bus can be divided into an address bus, a data bus, a control bus, etc. For ease of representation, Figure 2 Only one bidirectional arrow is used in the diagram, but this does not mean that there is only one bus or only one type of bus.

[0043] The memory is used to store the program. Specifically, the program may include a program code, and the program code includes a computer operation instruction. The memory may include a memory and a non-volatile memory, and provides instructions and data to the processor.

[0044] The processor reads the corresponding computer program from the non-volatile memory into the memory and then runs it, forming a wind power-based hydrogen collaborative production device at the logical level. The processor executes the program stored in the memory and is specifically used to execute any of the aforementioned wind power-based hydrogen collaborative production methods.

[0045] The above application Figure 1The embodiment shown discloses a wind power-based hydrogen collaborative production method that can be applied to a processor or implemented by a processor. The processor may be an integrated circuit chip with signal processing capabilities. In the implementation process, each step of the above method can be completed by an integrated logic circuit of hardware in the processor or an instruction in the form of software. The above processor may be a general-purpose processor, including a central processing unit (CPU), a network processor (NP), etc.; it may also be a digital signal processor (DSP), an application-specific integrated circuit (ASIC), a field-programmable gate array (FPGA) or other programmable logic devices, discrete gates or transistor logic devices, discrete hardware components. The methods, steps and logic block diagrams disclosed in the embodiments of the present application can be implemented or executed. The general-purpose processor may be a microprocessor or the processor may also be any conventional processor, etc. The steps of the method disclosed in the embodiment of the present application can be directly embodied as being executed by a hardware decoding processor, or executed by a combination of hardware and software modules in a decoding processor. The software module can be located in a storage medium mature in the art such as a random access memory, a flash memory, a read-only memory, a programmable read-only memory, or an electrically erasable programmable memory, a register, etc. The storage medium is located in the memory, and the processor reads the information in the memory and completes the steps of the above method in combination with its hardware.

[0046] The electronic device may also perform Figure 1 A wind power-based hydrogen production method Figure 1 The functions of the illustrated embodiment will not be described in detail in the embodiments of the present application.

[0047] An embodiment of the present application also proposes a computer-readable storage medium, which stores one or more programs, and the one or more programs include instructions. When the instructions are executed by an electronic device including multiple application programs, any one of the aforementioned wind power-based coordinated hydrogen production methods is executed.

[0048] Those skilled in the art will appreciate that the embodiments of the present application may be provided as methods, systems, or computer program products. Therefore, the present application may adopt the form of a complete hardware embodiment, a complete software embodiment, or an embodiment combining software and hardware. Moreover, the present application may adopt the form of a computer program product implemented on one or more computer-usable storage media (including but not limited to disk storage, CD-ROM, optical storage, etc.) containing computer-usable program codes.

[0049] The present application is described with reference to the flowcharts and / or block diagrams of the methods, devices (systems), and computer program products according to the embodiments of the present application. It should be understood that each process and / or box in the flowchart and / or block diagram, as well as the combination of the processes and / or boxes in the flowchart and / or block diagram, can be implemented by computer program instructions. These computer program instructions can be provided to a processor of a general-purpose computer, a special-purpose computer, an embedded processor, or other programmable data processing device to generate a machine, so that the instructions executed by the processor of the computer or other programmable data processing device generate instructions for implementing the processes in the flowchart and / or block diagram. Figure 1 A process or multiple processes and / or boxes Figure 1 A device that provides the functions specified in a block or multiple blocks.

[0050] These computer program instructions may also be stored in a computer-readable memory capable of directing a computer or other programmable data processing device to operate in a specific manner, so that the instructions stored in the computer-readable memory produce an article of manufacture comprising an instruction device, which implements the process Figure 1 A process or multiple processes and / or boxes Figure 1 A function specified in one or more boxes.

[0051] These computer program instructions can also be loaded onto a computer or other programmable data processing device so that a series of operating steps are executed on the computer or other programmable device to produce a computer-implemented process, thereby providing instructions for implementing the process in the computer or other programmable device. Figure 1 A process or multiple processes and / or boxes Figure 1 The steps for the functions specified in one or more boxes.

[0052] In a typical configuration, a computing device includes one or more processors (CPU), input / output interfaces, network interfaces, and memory.

[0053] Memory may include non-permanent storage in a computer-readable medium, in the form of random access memory (RAM) and / or non-volatile memory, such as read-only memory (ROM) or flash RAM. Memory is an example of a computer-readable medium.

[0054] Computer readable media include permanent and non-permanent, removable and non-removable media that can be implemented by any method or technology to store information. Information can be computer readable instructions, data structures, program modules or other data. Examples of computer storage media include, but are not limited to, phase change memory (PRAM), static random access memory (SRAM), dynamic random access memory (DRAM), other types of random access memory (RAM), read-only memory (ROM), electrically erasable programmable read-only memory (EEPROM), flash memory or other memory technology, compact disk read-only memory (CD-ROM), digital versatile disk (DVD) or other optical storage, magnetic cassettes, magnetic tape magnetic disk storage or other magnetic storage devices or any other non-transmission media that can be used to store information that can be accessed by a computing device. As defined herein, computer readable media does not include temporary computer readable media (transitory media), such as modulated data signals and carrier waves.

[0055] It should also be noted that the terms "include", "comprises" or any other variations thereof are intended to cover non-exclusive inclusion, so that a process, method, commodity or device including a series of elements includes not only those elements, but also other elements not explicitly listed, or also includes elements inherent to such process, method, commodity or device. In the absence of more restrictions, the elements defined by the sentence "comprises a ..." do not exclude the existence of other identical elements in the process, method, commodity or device including the elements.

[0056] Those skilled in the art will appreciate that the embodiments of the present application may be provided as methods, systems or computer program products. Therefore, the present application may take the form of a complete hardware embodiment, a complete software embodiment or an embodiment combining software and hardware. Moreover, the present application may take the form of a computer program product implemented on one or more computer-usable storage media (including but not limited to disk storage, CD-ROM, optical storage, etc.) containing computer-usable program codes.

[0057] The above is only an embodiment of the present application and is not intended to limit the present application. For those skilled in the art, the present application may have various changes and variations. Any modification, equivalent replacement, improvement, etc. made within the spirit and principle of the present application should be included in the scope of the claims of the present application.

Claims

1. A wind power-based hydrogen synergistic production method, characterized in that: The method is based on a coordinated hydrogen production device, the device comprising a first electrolyzer and a second electrolyzer arranged on the outer peripheral side of the first electrolyzer, the first electrolyzer and the second electrolyzer are isolated from each other in internal space, so that there is no material exchange between the first electrolyzer and the second electrolyzer, but there is heat exchange, the method comprises: Using the surplus electric energy generated by the wind turbine generator set but not fed into the power grid to heat the electrolyte in the second electrolytic cell; When the first condition is met, the electrodes in the second electrolytic cell are energized so that the current of the electrodes in the second electrolytic cell reaches the first current; the first condition includes one of the following: the duration of the wind turbine generator set being in a full-load state reaches a preset first duration, and the duration of the electrolyte heating in the second electrolytic cell reaches a preset second duration; the temperature of the electrolyte in the second electrolytic cell reaches a first reaction temperature, which is the reaction temperature of the second electrolytic cell that can achieve the highest efficiency and stable reaction under the condition of the first current; When the second condition is met, the current of the electrode in the second electrolytic cell is increased to the second current; the second condition includes one of the following: within a first time period after the first condition is met, the change in the instantaneous output power of the wind turbine generator set is less than a preset change threshold, and the oxygen content of the electrolyte in the second electrolytic cell reaches a preset oxygen content threshold; the temperature of the electrolyte in the second electrolytic cell reaches a second reaction temperature, and the second reaction temperature is the reaction temperature of the second electrolytic cell that can achieve the highest efficiency and stable reaction under the condition of the second current; If it is detected that the temperature of the electrolyte in the first electrolytic cell reaches the first reaction temperature, the electrodes in the first electrolytic cell are energized so that the current of the electrodes in the first electrolytic cell reaches the first current, so that the first electrolytic cell performs an electrolytic hydrogen production reaction.

2. The method according to claim 1, characterized in that: The method further comprises: When the third condition is met, stop energizing the electrodes in the first electrolytic cell; the third condition includes: the duration for which the change in the instantaneous output power of the wind turbine generator set is greater than the change threshold is greater than a preset third duration; the third duration is negatively correlated with the maximum single-unit capacity of the wind turbine generator set, negatively correlated with the total capacity of the wind turbine generator set, and positively correlated with the volume of the second electrolytic cell.

3. The method according to claim 1, characterized in that: The method further comprises: When a fourth condition is reached, powering the electrodes in the second electrolytic cell is stopped; the fourth condition includes: the temperature of the electrolyte in the first electrolytic cell is lower than the first reaction temperature.

4. The method according to claim 1, characterized in that: The method further comprises: The cooperative hydrogen production device also includes a thermal insulation layer; the thermal insulation layer is arranged on the side of the second electrolytic cell facing the external environment.

5. The method according to claim 1, characterized in that: The method further comprises: The first electrolytic cell and the second electrolytic cell are both electrolytic cells based on anion exchange membrane technology.

6. The method according to claim 5, characterized in that The method further comprises: The first reaction temperature is between 50 degrees Celsius and 70 degrees Celsius; The second reaction temperature is between 70 degrees Celsius and 90 degrees Celsius.

7. The method according to claim 1, characterized in that: The method further comprises: The capacity of the first electrolytic tank is smaller than the capacity of the second electrolytic tank.

8. The method according to claim 7, characterized in that: The method further comprises: According to the temperature of the electrolyte in the first electrolytic cell, plotting a temperature versus time curve; When the temperature change curve over time shows that the first electrolytic cell is in a heating state and the heating rate is greater than a preset rate threshold, the judgment of the first condition is performed; the rate threshold is negatively correlated with the difference in capacity between the first electrolytic cell and the second electrolytic cell.

9. An electronic device, comprising: processor; as well as A memory arranged to store computer executable instructions, which when executed cause the processor to perform the method of any one of claims 1 to 8.

10. A computer-readable storage medium storing one or more programs, which, when executed by an electronic device including a plurality of application programs, enables the electronic device to execute any one of the methods of claims 1 to 8.

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