Self-adaptive hydrogen production equipment temperature optimization control method and system

Abstract

The invention provides a self-adaptive hydrogen production equipment temperature optimization control method and system, and the method comprises the steps: collecting the current hydrogen production storage state of hydrogen production equipment, the current first temperature data of the hydrogen production equipment, and the second temperature data of the current environment, and generating the current temperature change information of the hydrogen production equipment; identifying temperature range information of each environment area, and identifying an abnormal area of the hydrogen production equipment; generating a temperature control strategy of each abnormal area through a temperature control strategy generation module, and collecting a temperature control adjustment result of each abnormal area; and adjusting a temperature control strategy of each abnormal area based on the temperature control adjustment result of each abnormal area, generating a target temperature control strategy of each abnormal area, adjusting temperature data of each abnormal area based on the temperature control strategy of each abnormal area, and returning to execute the above steps. By adopting the scheme, the temperature optimization control efficiency of the self-adaptive hydrogen production equipment can be improved.

Description

Technical Field

[0001] The present invention relates to the technical field of intelligent temperature optimization control, and in particular to an adaptive temperature optimization control method and system for hydrogen production equipment. Background Art

[0002] The hydrogen production equipment includes various hydrogen production structures, which include a hydrogen reaction structure, a hydrogen transmission structure, and a hydrogen storage structure. Among them, the hydrogen reaction structure is used to contact with water to generate hydrogen through electrochemical reaction, and transmit the hydrogen to the hydrogen storage structure through the hydrogen transmission structure for hydrogen storage. The operating state of the hydrogen production equipment is easily affected by the external environment, thereby affecting the stability of hydrogen production or storage. Generally, the factor with the greatest influence in the external environment is temperature. Changes in temperature will directly lead to abnormalities in the hydrogen production state and the hydrogen storage state, and there is even a risk of safety accidents, which may cause personal injury or property loss. Therefore, how to improve the temperature optimization control of the hydrogen production equipment is the current research focus.

[0003] The traditional method of temperature optimization control of hydrogen production equipment is to manually detect the temperature data of each hydrogen production structure of the hydrogen production equipment, and then adjust the temperature state of the hydrogen production equipment through circuit control or chip control, or even suspend the hydrogen production and storage process of the hydrogen production equipment to ensure the safe and normal operation of the hydrogen production equipment. However, this method has poor timeliness, low accuracy of manual control, and greatly affects the hydrogen production rate and hydrogen production efficiency, resulting in low efficiency of temperature optimization control of hydrogen production equipment. Summary of the invention

[0004] The main purpose of the present invention is to provide an adaptive hydrogen production equipment temperature optimization control method and system, aiming to solve the problem of the prior art that the hydrogen production equipment temperature optimization control efficiency is poor due to poor timeliness, low precision of manual control, and great influence on the hydrogen production rate and hydrogen production efficiency.

[0005] To achieve the above object, the present invention provides an adaptive temperature optimization control method for hydrogen production equipment, the method comprising:

[0006] Collecting the current hydrogen production storage state of the hydrogen production equipment, the current first temperature data of the hydrogen production equipment, and the second temperature data of the current environment, and generating the current temperature change information of the hydrogen production equipment based on the current first temperature data of the hydrogen production equipment;

[0007] Based on the second temperature data, identifying the temperature range information of each environmental area, and based on the current temperature change information and the current hydrogen production and storage state, identifying the abnormal area of ​​the hydrogen production equipment;

[0008] Based on the temperature range information of each of the environmental areas, a temperature control strategy generating module is used to generate a temperature control strategy for each of the abnormal areas, and after the temperature control strategy for each of the abnormal areas is executed by the temperature control adjustment module to adjust the temperature of each of the abnormal areas, a temperature control adjustment result for each of the abnormal areas is collected;

[0009] Based on the temperature control adjustment results of each abnormal area, the temperature control strategy of each abnormal area is adjusted, and the target temperature control strategy of each abnormal area is generated. Based on the temperature control strategy of each abnormal area, the temperature data of each abnormal area is adjusted, and the step of collecting the current hydrogen production storage state of the hydrogen production equipment, the current first temperature data of the hydrogen production equipment, and the second temperature data of the current environment is returned to execute.

[0010] Optionally, the generating current temperature change information of the hydrogen production equipment based on the current first temperature data of the hydrogen production equipment includes:

[0011] Splitting the current first temperature data of the hydrogen production equipment into sub-temperature data of each equipment area, and calculating the temperature change value between the sub-temperature data of each equipment area and the historical sub-temperature data of each equipment area;

[0012] According to the position range of each equipment area in the hydrogen production equipment, the temperature change values ​​of each equipment area are arranged and processed for temperature distribution to obtain the temperature change distribution information of each equipment area, and the temperature change distribution information of each equipment area is used as the current temperature change information of the hydrogen production equipment.

[0013] Optionally, the identifying the temperature range information of each environmental area based on the second temperature data includes:

[0014] Splitting the second temperature data into sub-temperature data of each environmental area at each moment, and performing distribution sorting processing on the sub-temperature data of each environmental area at each moment in chronological order to obtain temperature distribution information of each environmental area;

[0015] The temperature range of the temperature distribution information of each environmental area is identified to obtain the temperature range information of each environmental area.

[0016] Optionally, the identifying an abnormal area of ​​the hydrogen production equipment based on the current temperature change information and the current hydrogen production and storage state includes:

[0017] Based on the current hydrogen production storage state, identifying the structural operation state of each hydrogen production structure of the hydrogen production equipment, and based on the structural operation state of each hydrogen production structure, identifying an abnormal hydrogen production structure in each hydrogen production structure;

[0018] Based on the temperature change distribution information of each device area, identify the temperature change trend of each device area and the temperature range change trend of each device area, and based on the temperature change trend of each device area and the temperature range change trend of each device area, evaluate the temperature abnormality of each device area through the temperature evaluation strategy of each device area;

[0019] Screening the equipment area corresponding to the temperature abnormality degree greater than the temperature abnormality degree threshold as the first abnormal area, and screening the equipment area corresponding to each of the abnormal hydrogen production structures as the second abnormal area;

[0020] Based on the first abnormal region and the second abnormal region, each abnormal region of the hydrogen production equipment is identified.

[0021] Optionally, based on the temperature range information of each of the environmental areas, generating a temperature control strategy for each of the abnormal areas through a temperature control strategy generation module includes:

[0022] For each abnormal region, based on the temperature abnormality degree of the abnormal region, a temperature adjustment range of the abnormal region is calculated, and based on the temperature range change trend of the abnormal region and the temperature change trend of the abnormal region, a temperature adjustment direction of the abnormal region is identified;

[0023] Based on the temperature range information of each of the environmental areas and the temperature range change trend of the abnormal area, in each of the environmental areas, the target environmental area corresponding to the abnormal area is screened, and based on the temperature adjustment direction of the abnormal area, the temperature adjustment range of the abnormal area, and the temperature range information of the target environmental area, the water flow velocity range of the target environmental area and the water unit flow range of the target environmental area are generated through the temperature control strategy generation module;

[0024] The water flow velocity range of the target environmental area and the water unit flow range of the target environmental area are used as the temperature control strategy of the abnormal area.

[0025] Optionally, adjusting the temperature control strategy of each abnormal area based on the temperature control adjustment result of each abnormal area to generate a target temperature control strategy for each abnormal area includes:

[0026] For each abnormal region, based on the temperature control adjustment result of the abnormal region, identifying the new structural operation state of the hydrogen production structure corresponding to the abnormal region and the new temperature abnormality degree of the abnormal region;

[0027] Based on the new structural operation state of each of the hydrogen production structures, a new abnormal hydrogen production structure is screened, and based on the new temperature abnormality degree of each of the abnormal regions, a new second abnormal region corresponding to a temperature abnormality degree greater than a temperature abnormality degree threshold is screened;

[0028] Based on the new first abnormal area corresponding to each of the new abnormal hydrogen production structures and each of the new second abnormal areas, each new abnormal area of ​​the hydrogen production equipment is identified, and each of the new abnormal areas is replaced by each of the abnormal areas, and the temperature range information based on each of the environmental areas is returned to be executed, and a temperature control strategy for each of the abnormal areas is generated through a temperature control strategy generation module;

[0029] The temperature control strategy of each abnormal area is used as the target temperature control strategy of each new abnormal area.

[0030] To implement the above method, the present invention also provides an adaptive temperature optimization control device for hydrogen production equipment, the device comprising a control center module, a temperature control strategy generation module, and a temperature control adjustment module:

[0031] The control center module is connected to the temperature control strategy generation module and the temperature control adjustment module respectively, and the temperature control strategy generation module is connected to the temperature control adjustment module;

[0032] The control center module is arranged in the control mainboard of the hydrogen production equipment, and is used to receive the current hydrogen production storage state of the hydrogen production equipment, the current first temperature data of the hydrogen production equipment, and the second temperature data of the current environment collected by the sensors arranged in the hydrogen production equipment; based on the current first temperature data of the hydrogen production equipment, the current temperature change information of the hydrogen production equipment is generated; based on the second temperature data, the temperature range information of each environmental area is identified, and based on the current temperature change information and the current hydrogen production storage state, the abnormal area of ​​the hydrogen production equipment is identified; the control center module sends the temperature range information of each environmental area and the abnormal area of ​​the hydrogen production equipment to the temperature control strategy generation module;

[0033] The temperature control strategy generation module is arranged on the control mainboard of the hydrogen production equipment, and is used to receive the temperature range information of each of the environmental areas and the abnormal area of ​​the hydrogen production equipment sent by the control center module; based on the temperature range information of each of the environmental areas, generate the temperature control strategy of each of the abnormal areas, and send the temperature control strategy of each of the abnormal areas to the temperature control adjustment module;

[0034] The temperature control strategy generating module is further used to receive the temperature control adjustment results of each abnormal area sent by the temperature control adjustment module; based on the temperature control adjustment results of each abnormal area, adjust the temperature control strategy of each abnormal area, generate a target temperature control strategy for each abnormal area, and send the target temperature control strategy of each abnormal area to the temperature control adjustment module;

[0035] The temperature control and adjustment module includes a temperature control and adjustment unit arranged in the hydrogen storage area and a temperature control and adjustment unit arranged in the hydrogen production area, and is used to receive the temperature control strategy of each of the abnormal areas, and adjust the temperature data of each of the abnormal areas based on the temperature control strategy of each of the abnormal areas to obtain the temperature control and adjustment results of each of the abnormal areas; send the temperature control and adjustment results of each of the abnormal areas to the temperature control strategy generation module, and receive the target temperature control strategy of each of the abnormal areas transmitted by the temperature control strategy generation module; adjust the temperature data of each of the abnormal areas based on the target temperature control strategy of each of the abnormal areas, and send feedback iteration messages to the control center module;

[0036] The control center module is also used to return to execute the step of receiving the current hydrogen production storage state of the hydrogen production equipment collected by each sensor set in the hydrogen production equipment, the current first temperature data of the hydrogen production equipment, and the second temperature data of the current environment when receiving the feedback iteration message sent by the temperature control and adjustment module.

[0037] In addition, to achieve the above-mentioned purpose, the present invention also provides an adaptive hydrogen production equipment temperature optimization control system, the adaptive hydrogen production equipment temperature optimization control system said system comprises:

[0038] A collection module, used to collect the current hydrogen production storage state of the hydrogen production equipment, the current first temperature data of the hydrogen production equipment, and the second temperature data of the current environment, and generate the current temperature change information of the hydrogen production equipment based on the current first temperature data of the hydrogen production equipment;

[0039] an identification module, configured to identify the temperature range information of each environmental area based on the second temperature data, and to identify the abnormal area of ​​the hydrogen production equipment based on the current temperature change information and the current hydrogen production and storage state;

[0040] A generation module, configured to generate a temperature control strategy for each of the abnormal areas through a temperature control strategy generation module based on the temperature range information of each of the environmental areas, and collect temperature control adjustment results for each of the abnormal areas after the temperature control strategy for each of the abnormal areas is executed by the temperature control adjustment module to adjust the temperature of each of the abnormal areas;

[0041] The iteration module is used to adjust the temperature control strategy of each abnormal area based on the temperature control adjustment result of each abnormal area, generate a target temperature control strategy for each abnormal area, and adjust the temperature data of each abnormal area based on the temperature control strategy of each abnormal area, and return to execute the step of collecting the current hydrogen production storage state of the hydrogen production equipment, the current first temperature data of the hydrogen production equipment, and the second temperature data of the current environment.

[0042] Optionally, the acquisition module is specifically used to:

[0043] Splitting the current first temperature data of the hydrogen production equipment into sub-temperature data of each equipment area, and calculating the temperature change value between the sub-temperature data of each equipment area and the historical sub-temperature data of each equipment area;

[0044] According to the position range of each equipment area in the hydrogen production equipment, the temperature change values ​​of each equipment area are arranged and processed for temperature distribution to obtain the temperature change distribution information of each equipment area, and the temperature change distribution information of each equipment area is used as the current temperature change information of the hydrogen production equipment.

[0045] Optionally, the identification module is specifically used to:

[0046] Splitting the second temperature data into sub-temperature data of each environmental area at each moment, and performing distribution sorting processing on the sub-temperature data of each environmental area at each moment in chronological order to obtain temperature distribution information of each environmental area;

[0047] The temperature range of the temperature distribution information of each environmental area is identified to obtain the temperature range information of each environmental area.

[0048] Optionally, the identification module is specifically used to:

[0049] Based on the current hydrogen production storage state, identifying the structural operation state of each hydrogen production structure of the hydrogen production equipment, and based on the structural operation state of each hydrogen production structure, identifying an abnormal hydrogen production structure in each hydrogen production structure;

[0050] Based on the temperature change distribution information of each device area, identify the temperature change trend of each device area and the temperature range change trend of each device area, and based on the temperature change trend of each device area and the temperature range change trend of each device area, evaluate the temperature abnormality of each device area through the temperature evaluation strategy of each device area;

[0051] Screening the equipment area corresponding to the temperature abnormality degree greater than the temperature abnormality degree threshold as the first abnormal area, and screening the equipment area corresponding to each of the abnormal hydrogen production structures as the second abnormal area;

[0052] Based on the first abnormal region and the second abnormal region, each abnormal region of the hydrogen production equipment is identified.

[0053] Optionally, the generating module is specifically used for:

[0054] For each abnormal region, based on the temperature abnormality degree of the abnormal region, a temperature adjustment range of the abnormal region is calculated, and based on the temperature range change trend of the abnormal region and the temperature change trend of the abnormal region, a temperature adjustment direction of the abnormal region is identified;

[0055] Based on the temperature range information of each of the environmental areas and the temperature range change trend of the abnormal area, in each of the environmental areas, the target environmental area corresponding to the abnormal area is screened, and based on the temperature adjustment direction of the abnormal area, the temperature adjustment range of the abnormal area, and the temperature range information of the target environmental area, the water flow velocity range of the target environmental area and the water unit flow range of the target environmental area are generated through the temperature control strategy generation module;

[0056] The water flow velocity range of the target environmental area and the water unit flow range of the target environmental area are used as the temperature control strategy of the abnormal area.

[0057] Optionally, the iteration module is specifically used for:

[0058] For each abnormal region, based on the temperature control adjustment result of the abnormal region, identifying the new structural operation state of the hydrogen production structure corresponding to the abnormal region and the new temperature abnormality degree of the abnormal region;

[0059] Based on the new structural operation state of each of the hydrogen production structures, a new abnormal hydrogen production structure is screened, and based on the new temperature abnormality degree of each of the abnormal regions, a new second abnormal region corresponding to a temperature abnormality degree greater than a temperature abnormality degree threshold is screened;

[0060] Based on the new first abnormal area corresponding to each of the new abnormal hydrogen production structures and each of the new second abnormal areas, each new abnormal area of ​​the hydrogen production equipment is identified, and each of the new abnormal areas is replaced by each of the abnormal areas, and the temperature range information based on each of the environmental areas is returned to be executed, and a temperature control strategy for each of the abnormal areas is generated through a temperature control strategy generation module;

[0061] The temperature control strategy of each abnormal area is used as the target temperature control strategy of each new abnormal area.

[0062] The present invention provides an adaptive temperature optimization control method and system for hydrogen production equipment. The method comprises: collecting the current hydrogen production storage state of the hydrogen production equipment, the current first temperature data of the hydrogen production equipment, and the second temperature data of the current environment, and generating the current temperature change information of the hydrogen production equipment based on the current first temperature data of the hydrogen production equipment; identifying the temperature range information of each environmental area based on the second temperature data, and identifying the abnormal area of ​​the hydrogen production equipment based on the current temperature change information and the current hydrogen production storage state; based on the temperature range information of each environmental area, generating the temperature control strategy of each abnormal area through a temperature control strategy generation module, and after the temperature control strategy of each abnormal area is executed by the temperature control adjustment module to adjust the temperature of each abnormal area, collecting the temperature control adjustment result of each abnormal area; based on the temperature control adjustment result of each abnormal area, adjusting the temperature control strategy of each abnormal area, generating the target temperature control strategy of each abnormal area, and adjusting the temperature data of each abnormal area based on the temperature control strategy of each abnormal area, and returning to execute the step of collecting the current hydrogen production storage state of the hydrogen production equipment, the current first temperature data of the hydrogen production equipment, and the second temperature data of the current environment.

[0063] This scheme identifies the abnormal area of ​​the hydrogen production equipment by combining the current hydrogen production storage state of the hydrogen production equipment and the temperature data of the hydrogen production equipment, so that when identifying the abnormal area, the abnormal identification of the hydrogen production equipment can be carried out from the two perspectives of the current hydrogen production storage state of the hydrogen production equipment and the temperature data, thereby improving the accuracy and comprehensiveness of identifying the abnormal area. Then, this scheme combines the temperature control strategy generation module and the temperature control adjustment module to screen the environmental areas that can adjust the temperature of each abnormal area in each environmental area of ​​the current environment, thereby generating the temperature control strategy of each abnormal area, and adjusting the temperature control strategy of each abnormal area based on the temperature control adjustment results of each abnormal area, thereby improving the accuracy of temperature control of each abnormal area. Finally, this scheme realizes the intelligent temperature control of the hydrogen production equipment by adaptively adjusting the hydrogen production equipment through real-time acquisition and cyclic adjustment, which not only improves the accuracy of temperature control, but also effectively improves the timeliness of temperature control, thereby comprehensively improving the efficiency of adaptive temperature optimization control of hydrogen production equipment. BRIEF DESCRIPTION OF THE DRAWINGS

[0064] In order to more clearly illustrate the scheme in the present application, a brief introduction is given below to the drawings required for use in the description of the embodiments of the present application. Obviously, the drawings described below are some embodiments of the present application. For ordinary technicians in this field, other drawings can be obtained based on these drawings without paying any creative work.

[0065] Figure 1is a device structure diagram of a self-adaptive hydrogen production equipment temperature optimization control device provided by an embodiment of the present invention;

[0066] Figure 2 is a flow chart of an adaptive hydrogen production equipment temperature optimization control method provided by an embodiment of the present invention;

[0067] Figure 3 It is a structural schematic diagram of an adaptive temperature optimization control system for hydrogen production equipment provided in an embodiment of the present invention. DETAILED DESCRIPTION

[0068] The adaptive hydrogen production equipment temperature optimization control method provided by the embodiment of the present invention is applied to the adaptive hydrogen production equipment temperature optimization control system. Unless otherwise defined, all technical and scientific terms used in this article have the same meaning as those generally understood by technicians in the technical field of this application; the terms used in the specification of the application herein are only for the purpose of describing specific embodiments and are not intended to limit this application; the terms "including" and "having" in the specification and claims of this application and the above-mentioned figure descriptions and any variations thereof are intended to cover non-exclusive inclusions. The terms "first", "second", etc. in the specification and claims of this application or the above-mentioned figures are used to distinguish different objects, not to describe a specific order.

[0069] Reference to "embodiments" herein means that a particular feature, structure, or characteristic described in conjunction with the embodiments may be included in at least one embodiment of the present application. The appearance of the phrase in various locations in the specification does not necessarily refer to the same embodiment, nor is it an independent or alternative embodiment that is mutually exclusive with other embodiments. It is explicitly and implicitly understood by those skilled in the art that the embodiments described herein may be combined with other embodiments.

[0070] In order to enable those skilled in the art to better understand the solution of the present application, the technical solution in the embodiments of the present application will be clearly and completely described below in conjunction with the accompanying drawings.

[0071] The adaptive hydrogen production equipment temperature optimization control method provided in the embodiment of the present application can be applied to Figure 1In the adaptive temperature optimization control device for hydrogen production equipment shown, the device includes a control center module, a temperature control strategy generation module, and a temperature control adjustment module: the control center module is connected to the temperature control strategy generation module and the temperature control adjustment module respectively, and the temperature control strategy generation module is connected to the temperature control adjustment module. Among them, the control center module can be a terminal or a server, and can also identify a system including a terminal and a server, and is implemented through the interaction between the terminal and the server. Among them, the terminal can be but not limited to various personal computers, laptops, smart phones, tablet computers, etc. Among them, the terminal identifies the abnormal area of ​​the hydrogen production equipment by combining the current hydrogen production storage state of the hydrogen production equipment and the temperature data of the hydrogen production equipment, so that when identifying the abnormal area, the abnormal identification of the hydrogen production equipment can be performed from the two perspectives of the current hydrogen production storage state of the hydrogen production equipment and the temperature data, thereby improving the accuracy and comprehensiveness of identifying the abnormal area. Then, this scheme combines the temperature control strategy generation module and the temperature control adjustment module to select environmental areas that can adjust the temperature of each abnormal area in each environmental area of ​​the current environment, thereby generating a temperature control strategy for each abnormal area, and adjusting the temperature control strategy for each abnormal area based on the temperature control adjustment results of each abnormal area, thereby improving the accuracy of temperature control for each abnormal area. Finally, this scheme realizes the intelligent temperature control of the hydrogen production equipment by adaptively adjusting the hydrogen production equipment through real-time acquisition and cyclic adjustment, which not only improves the accuracy of temperature control, but also effectively improves the timeliness of temperature control, thereby comprehensively improving the temperature optimization control efficiency of the adaptive hydrogen production equipment.

[0072] In one embodiment, Figure 2 As shown, an adaptive temperature optimization control method for hydrogen production equipment is provided. Figure 1 The terminal of the control center is used as an example to illustrate the process, including the following steps:

[0073] Step S201, collecting the current hydrogen production storage state of the hydrogen production equipment, the current first temperature data of the hydrogen production equipment, and the second temperature data of the current environment, and generating the current temperature change information of the hydrogen production equipment based on the current first temperature data of the hydrogen production equipment.

[0074] In this embodiment, the terminal collects the current hydrogen production storage state of the hydrogen production equipment, the current first temperature data of the hydrogen production equipment, and the second temperature data of the current environment by receiving sensors set in each equipment area of ​​the hydrogen production equipment. Among them, the current hydrogen production storage state includes the structural operation state of each hydrogen production structure of the hydrogen production equipment. Among them, the hydrogen production structure includes a hydrogen reaction structure, a hydrogen transmission structure, and a hydrogen storage structure. The structural operation state characterizes the operation state of the hydrogen production structure, and the operation state includes but is not limited to a normal operation state, an unstable operation state, an inefficient operation state, an overclocking operation state, etc. The current first temperature data of the hydrogen production equipment includes sub-temperature data of each equipment area, and each hydrogen production structure corresponds to an equipment area. The second temperature data of the current environment includes sub-temperature data of each environmental area. The environmental area includes but is not limited to an environmental area corresponding to a water environment and an environmental area corresponding to an air environment. The environmental area corresponding to the water environment is the water source area collected by the current hydrogen production equipment during the hydrogen production reaction, and the environmental area corresponding to the air environment is the environmental area of ​​the non-water area where the current hydrogen production equipment is located. Finally, the terminal generates current temperature change information of the hydrogen production equipment based on the current first temperature data of the hydrogen production equipment. The current temperature change information includes temperature change distribution information of each equipment area of ​​the hydrogen production equipment. The specific temperature change distribution information will be described in detail later.

[0075] Step S202, based on the second temperature data, identifying the temperature range information of each environmental area, and based on the current temperature change information and the current hydrogen production and storage state, identifying the abnormal area of ​​the hydrogen production equipment.

[0076] In this embodiment, the terminal identifies the temperature range information of each environmental area based on the second temperature data, and identifies the abnormal area of ​​the hydrogen production equipment based on the current temperature change information and the current hydrogen production storage state. Among them, the abnormal area belongs to both the equipment area corresponding to the abnormal hydrogen production structure and the equipment area with abnormal temperature. The specific identification process will be described in detail later.

[0077] Step S203, based on the temperature range information of each environmental area, a temperature control strategy generation module is used to generate a temperature control strategy for each abnormal area, and after the temperature control adjustment module executes the temperature control strategy for each abnormal area to adjust the temperature of each abnormal area, the temperature control adjustment results of each abnormal area are collected.

[0078] In this embodiment, the terminal generates a temperature control strategy for each abnormal area through a temperature control strategy generation module based on the temperature range information of each environmental area, and collects the temperature control adjustment results of each abnormal area after executing the temperature control strategy of each abnormal area through the temperature control adjustment module to adjust the temperature of each abnormal area. The temperature control strategy includes the water flow velocity range of the environmental area where the temperature control is applied to the abnormal area, and the water unit flow range of the environmental area where the temperature control is applied to the abnormal area.

[0079] Step S204, based on the temperature control adjustment results of each abnormal area, adjust the temperature control strategy of each abnormal area, generate a target temperature control strategy for each abnormal area, and adjust the temperature data of each abnormal area based on the temperature control strategy of each abnormal area, and return to execute the step of collecting the current hydrogen production storage state of the hydrogen production equipment, the current first temperature data of the hydrogen production equipment, and the second temperature data of the current environment.

[0080] In this embodiment, the terminal adjusts the temperature control strategy of each abnormal area based on the temperature control adjustment results of each abnormal area, generates a target temperature control strategy for each abnormal area, and adjusts the temperature data of each abnormal area based on the temperature control strategy of each abnormal area, and returns to execute the step of collecting the current hydrogen production storage state of the hydrogen production equipment, the current first temperature data of the hydrogen production equipment, and the second temperature data of the current environment.

[0081] Based on the above scheme, by combining the current hydrogen production storage state of the hydrogen production equipment and the temperature data of the hydrogen production equipment, the abnormal area of ​​the hydrogen production equipment is identified, so that when identifying the abnormal area, the abnormal identification of the hydrogen production equipment can be carried out from the two perspectives of the current hydrogen production storage state of the hydrogen production equipment and the temperature data, thereby improving the accuracy and comprehensiveness of identifying the abnormal area. Then, this scheme combines the temperature control strategy generation module and the temperature control adjustment module to screen the environmental areas that can adjust the temperature of each abnormal area in each environmental area of ​​the current environment, thereby generating the temperature control strategy of each abnormal area, and adjusting the temperature control strategy of each abnormal area based on the temperature control adjustment results of each abnormal area, thereby improving the accuracy of temperature control of each abnormal area. Finally, this scheme realizes the intelligent temperature control of the hydrogen production equipment by adaptively adjusting the hydrogen production equipment through real-time acquisition and cyclic adjustment, which not only improves the accuracy of temperature control, but also effectively improves the timeliness of temperature control, thereby comprehensively improving the efficiency of adaptive temperature optimization control of hydrogen production equipment.

[0082] Optionally, based on the current first temperature data of the hydrogen production equipment, current temperature change information of the hydrogen production equipment is generated, including: splitting the current first temperature data of the hydrogen production equipment into sub-temperature data of each equipment area, and calculating the temperature change value between the sub-temperature data of each equipment area and the historical sub-temperature data of each equipment area; arranging the temperature change values ​​of each equipment area according to the position range of each equipment area in the hydrogen production equipment to obtain the temperature change distribution information of each equipment area, and using the temperature change distribution information of each equipment area as the current temperature change information of the hydrogen production equipment.

[0083] In this embodiment, the terminal splits the current first temperature data of the hydrogen production equipment into sub-temperature data of each equipment area, and calculates the temperature change value between the sub-temperature data of each equipment area and the historical sub-temperature data of each equipment area. The historical sub-temperature data of each equipment area is the sub-temperature data of each equipment area obtained when the temperature data was collected last time.

[0084] Then, the terminal arranges the temperature change values ​​of each equipment area according to the position range of each equipment area in the hydrogen production equipment, obtains the temperature change distribution information of each equipment area, and uses the temperature change distribution information of each equipment area as the current temperature change information of the hydrogen production equipment.

[0085] Based on the above scheme, the current temperature change information of the hydrogen production equipment is obtained by temperature difference calculation and then distribution arrangement, thereby improving the accuracy of the identified current temperature change information of the hydrogen production equipment.

[0086] Optionally, based on the second temperature data, the temperature range information of each environmental area is identified, including: splitting the second temperature data into sub-temperature data of each environmental area at each moment, and distributing and sorting the sub-temperature data of each environmental area at each moment in chronological order to obtain the temperature distribution information of each environmental area; identifying the temperature range of the temperature distribution information of each environmental area to obtain the temperature range information of each environmental area.

[0087] In this embodiment, the terminal splits the second temperature data into sub-temperature data at each moment of each environmental area, and distributes and sorts the sub-temperature data at each moment of each environmental area in chronological order to obtain temperature distribution information of each environmental area. The temperature data of the environmental area obtained includes sub-temperature data at each moment within a preset time interval. Then, the terminal identifies the temperature range of the temperature distribution information of each environmental area to obtain the temperature range information of each environmental area. The temperature range of the temperature distribution information is the average temperature value of each temperature peak value of the temperature distribution information and the range corresponding to the average temperature value of each temperature valley value.

[0088] Based on the above solution, the temperature data of each environmental area is distributed and sorted, and the temperature range information of each environmental area is identified, thereby improving the accuracy of identification.

[0089] Optionally, based on current temperature change information and current hydrogen production storage status, abnormal areas of the hydrogen production equipment are identified, including: based on the current hydrogen production storage status, the structural operating status of each hydrogen production structure of the hydrogen production equipment is identified, and based on the structural operating status of each hydrogen production structure, the abnormal hydrogen production structure in each hydrogen production structure is identified; based on the temperature change distribution information of each equipment area, the temperature change trend of each equipment area and the temperature range change trend of each equipment area are identified, and based on the temperature change trend of each equipment area and the temperature range change trend of each equipment area, the temperature abnormality of each equipment area is evaluated through the temperature evaluation strategy of each equipment area; the equipment area corresponding to the temperature abnormality degree greater than the temperature abnormality degree threshold is screened as the first abnormal area, and the equipment area corresponding to each abnormal hydrogen production structure is used as the second abnormal area; based on the first abnormal area and the second abnormal area, each abnormal area of ​​the hydrogen production equipment is identified.

[0090] In this embodiment, the terminal identifies the structural operation state of each hydrogen production structure of the hydrogen production equipment based on the current hydrogen production storage state, and identifies the abnormal hydrogen production structure in each hydrogen production structure based on the structural operation state of each hydrogen production structure. Among the structural operation states of each hydrogen production structure, the terminal selects the hydrogen production structure in the abnormal operation state as the abnormal hydrogen production structure, and the abnormal operation state includes but is not limited to an unstable operation state, an inefficient operation state, an overclocked operation state, etc.

[0091] Then, based on the temperature change distribution information of each device area, the terminal identifies the temperature change trend of each device area and the temperature range change trend of each device area, and based on the temperature change trend of each device area and the temperature range change trend of each device area, through the temperature evaluation strategy of each device area, evaluates the temperature abnormality of each device area. The temperature evaluation strategy of each device area includes the temperature change trend range corresponding to each temperature abnormality degree and the temperature range change trend range corresponding to each temperature abnormality degree. The terminal identifies the temperature range change trend range to which the temperature range change trend of each device area belongs, and the temperature change trend range to which the temperature change trend of each device area belongs, thereby determining the temperature abnormality degree of each device area.

[0092] The terminal selects the equipment area corresponding to the temperature anomaly degree greater than the temperature anomaly degree threshold as the first abnormal area, and the equipment area corresponding to each abnormal hydrogen production structure as the second abnormal area. Among them, the temperature anomaly degree threshold is the temperature anomaly degree threshold preset in the terminal. Finally, the terminal selects the equipment area that is both the first abnormal area and the second abnormal area as the abnormal area of ​​the hydrogen production equipment.

[0093] Based on the above scheme, the accuracy of screening is improved by screening the equipment area corresponding to the hydrogen production structure in abnormal operation state and the equipment area with abnormal temperature degree.

[0094] Optionally, based on the temperature range information of each environmental area, a temperature control strategy for each abnormal area is generated through a temperature control strategy generation module, including: for each abnormal area, based on the degree of temperature abnormality in the abnormal area, calculating the temperature adjustment range of the abnormal area, and identifying the temperature adjustment direction of the abnormal area based on the temperature range change trend of the abnormal area and the temperature change trend of the abnormal area; based on the temperature range information of each environmental area and the temperature range change trend of the abnormal area, in each environmental area, screening the target environmental area corresponding to the abnormal area, and based on the temperature adjustment direction of the abnormal area, the temperature adjustment range of the abnormal area, and the temperature range information of the target environmental area, generating a water flow velocity range of the target environmental area and a water unit flow range of the target environmental area through a temperature control strategy generation module; using the water flow velocity range of the target environmental area and the water unit flow range of the target environmental area as the temperature control strategy for the abnormal area.

[0095] In this embodiment, the terminal calculates the temperature adjustment range of each abnormal area based on the temperature abnormality of the abnormal area, and identifies the temperature adjustment direction of the abnormal area based on the temperature range change trend of the abnormal area and the temperature change trend of the abnormal area. Then, based on the temperature range information of each environmental area and the temperature range change trend of the abnormal area, the terminal screens the target environmental area corresponding to the abnormal area in each environmental area. Among them, the deviation value between the temperature range information of the target environmental area and the temperature range information of the abnormal area is the largest, and the direction of the deviation value is the same as the temperature adjustment direction of the abnormal area. For example, the temperature adjustment direction is cooling adjustment, and the direction of the deviation value is that the temperature range information of the target environmental area is lower than the temperature range information of the abnormal area.

[0096] Based on the temperature adjustment direction of the abnormal area, the temperature adjustment range of the abnormal area, and the temperature range information of the target environment area, the terminal generates the water flow velocity range of the target environment area and the water unit flow range of the target environment area through the temperature control strategy generation module. Among them, the temperature control strategy generation module includes a temperature adjustment algorithm, which can calculate the water flow velocity range and the water unit flow range based on the temperature adjustment range. The temperature adjustment algorithm includes the ratio of the water flow velocity range to the temperature change degree, and the ratio of the water unit flow range to the temperature change rate. The temperature adjustment range includes the temperature change degree range that needs to be adjusted and the temperature adjustment time range. Then, based on the temperature adjustment range of the abnormal area, the terminal calculates the water flow velocity range and the water unit flow range of the target environment area through the temperature adjustment algorithm. Finally, the terminal uses the water flow velocity range of the target environment area and the water unit flow range of the target environment area as the temperature control strategy of the abnormal area. Among them, the temperature adjustment algorithm is a proportional algorithm, and the proportional value of the proportional algorithm is the first proportional value of the water flow velocity range corresponding to the temperature adjustment range, and the second proportional value of the water unit flow range corresponding to each temperature adjustment range.

[0097] Based on the above scheme, by identifying the temperature adjustment range and temperature adjustment direction, the water flow velocity range and water unit flow range of each target environmental area are generated, thereby improving the control accuracy of the temperature control strategy for abnormal areas.

[0098] Optionally, based on the temperature control adjustment results of each abnormal area, the temperature control strategy of each abnormal area is adjusted to generate a target temperature control strategy for each abnormal area, including: for each abnormal area, based on the temperature control adjustment results of the abnormal area, identifying the new structural operating state of the hydrogen production structure corresponding to the abnormal area and the new temperature abnormality degree of the abnormal area; based on the new structural operating state of each hydrogen production structure, screening new abnormal hydrogen production structures, and based on the new temperature abnormality degree of each abnormal area, screening new second abnormal areas corresponding to the temperature abnormality degree greater than the temperature abnormality degree threshold; based on the new first abnormal area corresponding to each new abnormal hydrogen production structure, and each new second abnormal area, identifying each new abnormal area of ​​the hydrogen production equipment, and replacing each abnormal area with each new abnormal area, returning to execute based on the temperature range information of each environmental area, and generating a temperature control strategy for each abnormal area through a temperature control strategy generation module; using the temperature control strategy of each abnormal area as the target temperature control strategy for each new abnormal area.

[0099] In this embodiment, the terminal identifies the new structural operation state of the hydrogen production structure corresponding to the abnormal area and the new temperature abnormality degree of the abnormal area based on the temperature control adjustment result of the abnormal area for each abnormal area. Then, the terminal screens the new abnormal hydrogen production structure based on the new structural operation state of each hydrogen production structure, and screens the new second abnormal area corresponding to the temperature abnormality degree greater than the temperature abnormality degree threshold based on the new temperature abnormality degree of each abnormal area. After that, the terminal identifies each new abnormal area of ​​the hydrogen production equipment based on the new first abnormal area corresponding to each new abnormal hydrogen production structure and each new second abnormal area, and replaces each abnormal area with each new abnormal area, returns to execute the temperature range information based on each environmental area, and generates a new temperature control strategy for each abnormal area through the temperature control strategy generation module. Finally, the terminal uses the new temperature control strategy of each abnormal area as the target temperature control strategy of each new abnormal area. This step is a process of cyclically iteratively optimizing the temperature control strategy of each abnormal area, but in actual operation, the specific execution method of each step is the same as the execution method of each identical step described above, so this scheme is not redundantly described.

[0100] Based on the above solution, the temperature control accuracy of the hydrogen production equipment is improved by iteratively adjusting the temperature control strategy.

[0101] In one embodiment, Figure 1 As shown, an adaptive temperature optimization control device for hydrogen production equipment is provided, characterized in that the device includes a control center module, a temperature control strategy generation module, and a temperature control adjustment module:

[0102] The control center module is connected to the temperature control strategy generation module and the temperature control adjustment module respectively, and the temperature control strategy generation module is connected to the temperature control adjustment module.

[0103] The control center module is arranged in the control mainboard of the hydrogen production equipment, and is used to receive the current hydrogen production storage state of the hydrogen production equipment, the current first temperature data of the hydrogen production equipment, and the second temperature data of the current environment collected by the sensors arranged in the hydrogen production equipment; based on the current first temperature data of the hydrogen production equipment, the current temperature change information of the hydrogen production equipment is generated; based on the second temperature data, the temperature range information of each environmental area is identified, and based on the current temperature change information and the current hydrogen production storage state, the abnormal area of ​​the hydrogen production equipment is identified; the control center module sends the temperature range information of each environmental area and the abnormal area of ​​the hydrogen production equipment to the temperature control strategy generation module. Among them, the control center module can be a terminal, a server, or a system combining a terminal and a server connected to the control mainboard of the hydrogen production equipment.

[0104] The temperature control strategy generation module is arranged on the control mainboard of the hydrogen production equipment, and is used to receive the temperature range information of each environmental area and the abnormal area of ​​the hydrogen production equipment sent by the control center module; based on the temperature range information of each environmental area, the temperature control strategy of each abnormal area is generated, and the temperature control strategy of each abnormal area is sent to the temperature control adjustment module. The temperature control strategy generation module can be a hardware structure such as a control chip arranged on the control mainboard, or a control program unit arranged in the mainboard chip of the control mainboard.

[0105] The temperature control strategy generation module is also used to receive the temperature control adjustment results of each abnormal area sent by the temperature control adjustment module; based on the temperature control adjustment results of each abnormal area, adjust the temperature control strategy of each abnormal area, generate the target temperature control strategy of each abnormal area, and send the target temperature control strategy of each abnormal area to the temperature control adjustment module.

[0106] The temperature control and adjustment module includes a temperature control and adjustment unit arranged in the hydrogen storage area and a temperature control and adjustment unit arranged in the hydrogen production area, and is used to receive the temperature control strategy of each abnormal area, adjust the temperature data of each abnormal area based on the temperature control strategy of each abnormal area, and obtain the temperature control and adjustment results of each abnormal area; send the temperature control and adjustment results of each abnormal area to the temperature control strategy generation module, and receive the target temperature control strategy of each abnormal area transmitted by the temperature control strategy generation module; adjust the temperature data of each abnormal area based on the target temperature control strategy of each abnormal area, and send feedback iteration messages to the control center module. Among them, the temperature control and adjustment unit arranged in the hydrogen storage area / hydrogen production area is a temperature control and adjustment unit that collects water sources from different environmental areas and performs water cooling / water bath heating. Among them, each temperature control and adjustment unit includes a plurality of water cooling / water bath heating pipes arranged in a spiral on the surface of the hydrogen storage area / hydrogen production area. When water flow in a water environment is used for water cooling / water bath heating, the temperature control and regulation module directly obtains the water flow used for water cooling / water bath heating from the water area where hydrogen is produced by the current hydrogen production equipment. When water flow in an air environment is used for water cooling / water bath heating, the temperature control and regulation module obtains the water flow used for water cooling / water bath heating from the water body stored in the hydrogen production equipment.

[0107] The control center module is also used to return to execute the step of receiving the current hydrogen production storage state of the hydrogen production equipment, the current first temperature data of the hydrogen production equipment, and the second temperature data of the current environment collected by the sensors set in the hydrogen production equipment when receiving the feedback iteration message sent by the temperature control and adjustment module.

[0108] It should be understood that, although the various steps in the flowcharts involved in the above-mentioned embodiments are displayed in sequence according to the indication of the arrows, these steps are not necessarily executed in sequence according to the order indicated by the arrows. Unless there is a clear explanation in this article, the execution of these steps does not have a strict order restriction, and these steps can be executed in other orders. Moreover, at least a part of the steps in the flowcharts involved in the above-mentioned embodiments can include multiple steps or multiple stages, and these steps or stages are not necessarily executed at the same time, but can be executed at different times, and the execution order of these steps or stages is not necessarily to be carried out in sequence, but can be executed in turn or alternately with other steps or at least a part of the steps or stages in other steps.

[0109] Based on the same inventive concept, the embodiment of the present application also provides an adaptive hydrogen production equipment temperature optimization control system for implementing the adaptive hydrogen production equipment temperature optimization control method involved above. The implementation scheme for solving the problem provided by the system is similar to the implementation scheme recorded in the above method, so the specific limitations in one or more adaptive hydrogen production equipment temperature optimization control system embodiments provided below can refer to the limitations of the adaptive hydrogen production equipment temperature optimization control method above, and will not be repeated here.

[0110] Further references Figure 3 , as a response to the above Figure 2 The implementation of the method shown in the figure, the present application provides an embodiment of an adaptive hydrogen production equipment temperature optimization control system 300, the adaptive hydrogen production equipment temperature optimization control system system includes a collection module 310, an identification module 320, a generation module 330 and an iteration module 340, wherein:

[0111] The acquisition module 310 is used to acquire the current hydrogen production storage state of the hydrogen production equipment, the current first temperature data of the hydrogen production equipment, and the second temperature data of the current environment, and generate the current temperature change information of the hydrogen production equipment based on the current first temperature data of the hydrogen production equipment;

[0112] An identification module 320, configured to identify the temperature range information of each environmental area based on the second temperature data, and to identify the abnormal area of ​​the hydrogen production equipment based on the current temperature change information and the current hydrogen production and storage state;

[0113] A generating module 330 is used to generate a temperature control strategy for each of the abnormal areas through a temperature control strategy generating module based on the temperature range information of each of the environmental areas, and collect temperature control adjustment results for each of the abnormal areas after the temperature control strategy for each of the abnormal areas is executed by the temperature control adjustment module to adjust the temperature of each of the abnormal areas;

[0114] The iteration module 340 is used to adjust the temperature control strategy of each abnormal area based on the temperature control adjustment result of each abnormal area, generate a target temperature control strategy for each abnormal area, and adjust the temperature data of each abnormal area based on the temperature control strategy of each abnormal area, and return to execute the step of collecting the current hydrogen production storage state of the hydrogen production equipment, the current first temperature data of the hydrogen production equipment, and the second temperature data of the current environment.

[0115] Optionally, the acquisition module 310 is specifically used for:

[0116] Splitting the current first temperature data of the hydrogen production equipment into sub-temperature data of each equipment area, and calculating the temperature change value between the sub-temperature data of each equipment area and the historical sub-temperature data of each equipment area;

[0117] According to the position range of each equipment area in the hydrogen production equipment, the temperature change values ​​of each equipment area are arranged and processed for temperature distribution to obtain the temperature change distribution information of each equipment area, and the temperature change distribution information of each equipment area is used as the current temperature change information of the hydrogen production equipment.

[0118] Optionally, the identification module 320 is specifically configured to:

[0119] Splitting the second temperature data into sub-temperature data of each environmental area at each moment, and performing distribution sorting processing on the sub-temperature data of each environmental area at each moment in chronological order to obtain temperature distribution information of each environmental area;

[0120] The temperature range of the temperature distribution information of each environmental area is identified to obtain the temperature range information of each environmental area.

[0121] Optionally, the identification module 320 is specifically configured to:

[0122] Based on the current hydrogen production storage state, identifying the structural operation state of each hydrogen production structure of the hydrogen production equipment, and based on the structural operation state of each hydrogen production structure, identifying an abnormal hydrogen production structure in each hydrogen production structure;

[0123] Based on the temperature change distribution information of each device area, identify the temperature change trend of each device area and the temperature range change trend of each device area, and based on the temperature change trend of each device area and the temperature range change trend of each device area, evaluate the temperature abnormality of each device area through the temperature evaluation strategy of each device area;

[0124] Screening the equipment area corresponding to the temperature abnormality degree greater than the temperature abnormality degree threshold as the first abnormal area, and screening the equipment area corresponding to each of the abnormal hydrogen production structures as the second abnormal area;

[0125] Based on the first abnormal region and the second abnormal region, each abnormal region of the hydrogen production equipment is identified.

[0126] Optionally, the generating module 330 is specifically configured to:

[0127] For each abnormal region, based on the temperature abnormality degree of the abnormal region, a temperature adjustment range of the abnormal region is calculated, and based on the temperature range change trend of the abnormal region and the temperature change trend of the abnormal region, a temperature adjustment direction of the abnormal region is identified;

[0128] Based on the temperature range information of each of the environmental areas and the temperature range change trend of the abnormal area, in each of the environmental areas, the target environmental area corresponding to the abnormal area is screened, and based on the temperature adjustment direction of the abnormal area, the temperature adjustment range of the abnormal area, and the temperature range information of the target environmental area, the water flow velocity range of the target environmental area and the water unit flow range of the target environmental area are generated through the temperature control strategy generation module;

[0129] The water flow velocity range of the target environmental area and the water unit flow range of the target environmental area are used as the temperature control strategy of the abnormal area.

[0130] Optionally, the iteration module 340 is specifically configured to:

[0131] For each abnormal region, based on the temperature control adjustment result of the abnormal region, identifying the new structural operation state of the hydrogen production structure corresponding to the abnormal region and the new temperature abnormality degree of the abnormal region;

[0132] Based on the new structural operation state of each of the hydrogen production structures, a new abnormal hydrogen production structure is screened, and based on the new temperature abnormality degree of each of the abnormal regions, a new second abnormal region corresponding to a temperature abnormality degree greater than a temperature abnormality degree threshold is screened;

[0133] Based on the new first abnormal area corresponding to each of the new abnormal hydrogen production structures and each of the new second abnormal areas, each new abnormal area of ​​the hydrogen production equipment is identified, and each of the new abnormal areas is replaced by each of the abnormal areas, and the temperature range information based on each of the environmental areas is returned to be executed, and a temperature control strategy for each of the abnormal areas is generated through a temperature control strategy generation module;

[0134] The temperature control strategy of each abnormal area is used as the target temperature control strategy of each new abnormal area.

[0135] Each module in the above-mentioned adaptive hydrogen production equipment temperature optimization control system can be implemented in whole or in part by software, hardware and a combination thereof. Each of the above-mentioned modules can be embedded in or independent of a processor in a computer device in the form of hardware, or can be stored in a memory in a computer device in the form of software, so that the processor can call and execute the operations corresponding to each of the above modules.

[0136] It should be noted that the user information (including but not limited to user device information, user personal information, etc.) and data (including but not limited to data used for analysis, stored data, displayed data, etc.) involved in this application are all information and data authorized by the user or fully authorized by all parties.

[0137] Those of ordinary skill in the art can understand that all or part of the processes in the above-mentioned embodiment methods can be completed by instructing the relevant hardware through a computer program, and the computer program can be stored in a non-volatile computer-readable storage medium. When the computer program is executed, it can include the processes of the embodiments of the above-mentioned methods. Among them, any reference to the memory, database or other medium used in the embodiments provided in the present application can include at least one of non-volatile and volatile memory. Non-volatile memory can include read-only memory (ROM), magnetic tape, floppy disk, flash memory, optical memory, high-density embedded non-volatile memory, resistive random access memory (ReRAM), magnetic random access memory (MRAM), ferroelectric random access memory (FRAM), phase change memory (PCM), graphene memory, etc. Volatile memory can include random access memory (RAM) or external cache memory, etc. As an illustration and not limitation, RAM can be in various forms, such as static random access memory (SRAM) or dynamic random access memory (DRAM). The database involved in each embodiment provided in this application may include at least one of a relational database and a non-relational database. Non-relational databases may include distributed databases based on blockchains, etc., but are not limited to this. The processor involved in each embodiment provided in this application may be a general-purpose processor, a central processing unit, a graphics processor, a digital signal processor, a programmable logic device, a data processing logic device based on quantum computing, etc., but are not limited to this.

[0138] The technical features of the above embodiments may be combined arbitrarily. To make the description concise, not all possible combinations of the technical features in the above embodiments are described. However, as long as there is no contradiction in the combination of these technical features, they should be considered to be within the scope of this specification.

[0139] The above-described embodiments only express several implementation methods of the present application, and the descriptions thereof are relatively specific and detailed, but they cannot be understood as limiting the scope of the present application. It should be pointed out that, for a person of ordinary skill in the art, several variations and improvements can be made without departing from the concept of the present application, and these all belong to the protection scope of the present application. Therefore, the protection scope of the present application shall be subject to the attached claims.

Claims

1. An adaptive temperature optimization control method for hydrogen production equipment, characterized in that: The method comprises: Collecting the current hydrogen production storage state of the hydrogen production equipment, the current first temperature data of the hydrogen production equipment, and the second temperature data of the current environment, and generating the current temperature change information of the hydrogen production equipment based on the current first temperature data of the hydrogen production equipment; Based on the second temperature data, identifying the temperature range information of each environmental area, and based on the current temperature change information and the current hydrogen production and storage state, identifying the abnormal area of ​​the hydrogen production equipment; Based on the temperature range information of each of the environmental areas, a temperature control strategy generating module is used to generate a temperature control strategy for each of the abnormal areas, and after the temperature control strategy for each of the abnormal areas is executed by the temperature control adjustment module to adjust the temperature of each of the abnormal areas, a temperature control adjustment result for each of the abnormal areas is collected; Based on the temperature control adjustment results of each abnormal area, the temperature control strategy of each abnormal area is adjusted, and the target temperature control strategy of each abnormal area is generated. Based on the temperature control strategy of each abnormal area, the temperature data of each abnormal area is adjusted, and the step of collecting the current hydrogen production storage state of the hydrogen production equipment, the current first temperature data of the hydrogen production equipment, and the second temperature data of the current environment is returned to execute.

2. The method according to claim 1, characterized in that The step of generating current temperature change information of the hydrogen production equipment based on the current first temperature data of the hydrogen production equipment comprises: Splitting the current first temperature data of the hydrogen production equipment into sub-temperature data of each equipment area, and calculating the temperature change value between the sub-temperature data of each equipment area and the historical sub-temperature data of each equipment area; According to the position range of each equipment area in the hydrogen production equipment, the temperature change values ​​of each equipment area are arranged and processed for temperature distribution to obtain the temperature change distribution information of each equipment area, and the temperature change distribution information of each equipment area is used as the current temperature change information of the hydrogen production equipment.

3. The method according to claim 2, characterized in that The identifying the temperature range information of each environmental area based on the second temperature data includes: Splitting the second temperature data into sub-temperature data of each environmental area at each moment, and performing distribution sorting processing on the sub-temperature data of each environmental area at each moment in chronological order to obtain temperature distribution information of each environmental area; The temperature range of the temperature distribution information of each environmental area is identified to obtain the temperature range information of each environmental area.

4. The method according to claim 2, characterized in that: The identifying the abnormal area of ​​the hydrogen production equipment based on the current temperature change information and the current hydrogen production and storage state includes: Based on the current hydrogen production storage state, identifying the structural operation state of each hydrogen production structure of the hydrogen production equipment, and based on the structural operation state of each hydrogen production structure, identifying an abnormal hydrogen production structure in each hydrogen production structure; Based on the temperature change distribution information of each device area, identify the temperature change trend of each device area and the temperature range change trend of each device area, and based on the temperature change trend of each device area and the temperature range change trend of each device area, evaluate the temperature abnormality of each device area through the temperature evaluation strategy of each device area; Screening the equipment area corresponding to the temperature abnormality degree greater than the temperature abnormality degree threshold as the first abnormal area, and screening the equipment area corresponding to each of the abnormal hydrogen production structures as the second abnormal area; Based on the first abnormal region and the second abnormal region, each abnormal region of the hydrogen production equipment is identified.

5. The method according to claim 4, characterized in that The temperature control strategy generation module generates a temperature control strategy for each abnormal area based on the temperature range information of each environmental area, including: For each abnormal region, based on the temperature abnormality degree of the abnormal region, a temperature adjustment range of the abnormal region is calculated, and based on the temperature range change trend of the abnormal region and the temperature change trend of the abnormal region, a temperature adjustment direction of the abnormal region is identified; Based on the temperature range information of each of the environmental areas and the temperature range change trend of the abnormal area, in each of the environmental areas, the target environmental area corresponding to the abnormal area is screened, and based on the temperature adjustment direction of the abnormal area, the temperature adjustment range of the abnormal area, and the temperature range information of the target environmental area, the water flow velocity range of the target environmental area and the water unit flow range of the target environmental area are generated through the temperature control strategy generation module; The water flow velocity range of the target environmental area and the water unit flow range of the target environmental area are used as the temperature control strategy of the abnormal area.

6. The method according to claim 5, characterized in that The step of adjusting the temperature control strategy of each abnormal area based on the temperature control adjustment result of each abnormal area and generating a target temperature control strategy of each abnormal area includes: For each abnormal region, based on the temperature control adjustment result of the abnormal region, identifying the new structural operation state of the hydrogen production structure corresponding to the abnormal region and the new temperature abnormality degree of the abnormal region; Based on the new structural operation state of each of the hydrogen production structures, a new abnormal hydrogen production structure is screened, and based on the new temperature abnormality degree of each of the abnormal regions, a new second abnormal region corresponding to a temperature abnormality degree greater than a temperature abnormality degree threshold is screened; Based on the new first abnormal area corresponding to each of the new abnormal hydrogen production structures and each of the new second abnormal areas, each new abnormal area of ​​the hydrogen production equipment is identified, and each of the new abnormal areas is replaced by each of the abnormal areas, and the temperature range information based on each of the environmental areas is returned to be executed, and a temperature control strategy for each of the abnormal areas is generated through a temperature control strategy generation module; The temperature control strategy of each abnormal area is used as the target temperature control strategy of each new abnormal area.

7. An adaptive temperature optimization control device for hydrogen production equipment, characterized in that: The device includes a control center module, a temperature control strategy generation module, and a temperature control adjustment module: The control center module is connected to the temperature control strategy generation module and the temperature control adjustment module respectively, and the temperature control strategy generation module is connected to the temperature control adjustment module; The control center module is arranged in the control mainboard of the hydrogen production equipment, and is used to receive the current hydrogen production storage state of the hydrogen production equipment collected by the sensors arranged in the hydrogen production equipment, the current first temperature data of the hydrogen production equipment, and the second temperature data of the current environment; generating current temperature change information of the hydrogen production equipment based on the current first temperature data of the hydrogen production equipment; Based on the second temperature data, the temperature range information of each environmental area is identified, and based on the current temperature change information and the current hydrogen production storage state, the abnormal area of ​​the hydrogen production equipment is identified; the control center module sends the temperature range information of each environmental area and the abnormal area of ​​the hydrogen production equipment to the temperature control strategy generation module; The temperature control strategy generation module is arranged on the control mainboard of the hydrogen production equipment, and is used to receive the temperature range information of each of the environmental areas and the abnormal area of ​​the hydrogen production equipment sent by the control center module; based on the temperature range information of each of the environmental areas, generate the temperature control strategy of each of the abnormal areas, and send the temperature control strategy of each of the abnormal areas to the temperature control adjustment module; The temperature control strategy generating module is further used to receive the temperature control adjustment results of each abnormal area sent by the temperature control adjustment module; based on the temperature control adjustment results of each abnormal area, adjust the temperature control strategy of each abnormal area, generate a target temperature control strategy for each abnormal area, and send the target temperature control strategy of each abnormal area to the temperature control adjustment module; The temperature control and adjustment module includes a temperature control and adjustment unit arranged in the hydrogen storage area and a temperature control and adjustment unit arranged in the hydrogen production area, and is used to receive the temperature control strategy of each of the abnormal areas, and adjust the temperature data of each of the abnormal areas based on the temperature control strategy of each of the abnormal areas to obtain the temperature control and adjustment results of each of the abnormal areas; send the temperature control and adjustment results of each of the abnormal areas to the temperature control strategy generation module, and receive the target temperature control strategy of each of the abnormal areas transmitted by the temperature control strategy generation module; Based on the target temperature control strategy of each abnormal area, adjust the temperature data of each abnormal area, and send a feedback iteration message to the control center module; The control center module is also used to return to execute the step of receiving the current hydrogen production storage state of the hydrogen production equipment collected by each sensor set in the hydrogen production equipment, the current first temperature data of the hydrogen production equipment, and the second temperature data of the current environment when receiving the feedback iteration message sent by the temperature control and adjustment module.

8. An adaptive temperature optimization control system for hydrogen production equipment, characterized in that: The system comprises: A collection module, used to collect the current hydrogen production storage state of the hydrogen production equipment, the current first temperature data of the hydrogen production equipment, and the second temperature data of the current environment, and generate the current temperature change information of the hydrogen production equipment based on the current first temperature data of the hydrogen production equipment; an identification module, configured to identify the temperature range information of each environmental area based on the second temperature data, and to identify the abnormal area of ​​the hydrogen production equipment based on the current temperature change information and the current hydrogen production and storage state; A generation module, configured to generate a temperature control strategy for each of the abnormal areas through a temperature control strategy generation module based on the temperature range information of each of the environmental areas, and collect temperature control adjustment results for each of the abnormal areas after the temperature control strategy for each of the abnormal areas is executed by the temperature control adjustment module to adjust the temperature of each of the abnormal areas; The iteration module is used to adjust the temperature control strategy of each abnormal area based on the temperature control adjustment result of each abnormal area, generate a target temperature control strategy for each abnormal area, and adjust the temperature data of each abnormal area based on the temperature control strategy of each abnormal area, and return to execute the step of collecting the current hydrogen production storage state of the hydrogen production equipment, the current first temperature data of the hydrogen production equipment, and the second temperature data of the current environment.

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