CN114914492B - Local voltage detection device of fuel cell system and detection analysis method thereof - Google Patents
Local voltage detection device of fuel cell system and detection analysis method thereof Download PDFInfo
- Publication number
- CN114914492B CN114914492B CN202210567954.5A CN202210567954A CN114914492B CN 114914492 B CN114914492 B CN 114914492B CN 202210567954 A CN202210567954 A CN 202210567954A CN 114914492 B CN114914492 B CN 114914492B
- Authority
- CN
- China
- Prior art keywords
- fuel cell
- cell stack
- local
- voltage
- instantaneous voltages
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 239000000446 fuel Substances 0.000 title claims abstract description 189
- 238000001514 detection method Methods 0.000 title claims abstract description 34
- 238000004458 analytical method Methods 0.000 title claims abstract description 14
- 238000006243 chemical reaction Methods 0.000 claims abstract description 29
- 239000000523 sample Substances 0.000 claims abstract description 24
- 238000000034 method Methods 0.000 claims abstract description 19
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 34
- 239000001257 hydrogen Substances 0.000 claims description 34
- 229910052739 hydrogen Inorganic materials 0.000 claims description 34
- 230000001276 controlling effect Effects 0.000 claims description 13
- 230000017525 heat dissipation Effects 0.000 claims description 4
- 230000006698 induction Effects 0.000 claims description 4
- 230000001105 regulatory effect Effects 0.000 claims description 3
- 238000012216 screening Methods 0.000 claims 2
- 230000033228 biological regulation Effects 0.000 claims 1
- 238000011217 control strategy Methods 0.000 abstract description 2
- 238000010586 diagram Methods 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000010835 comparative analysis Methods 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04298—Processes for controlling fuel cells or fuel cell systems
- H01M8/04313—Processes for controlling fuel cells or fuel cell systems characterised by the detection or assessment of variables; characterised by the detection or assessment of failure or abnormal function
- H01M8/04537—Electric variables
- H01M8/04544—Voltage
- H01M8/04559—Voltage of fuel cell stacks
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04298—Processes for controlling fuel cells or fuel cell systems
- H01M8/04992—Processes for controlling fuel cells or fuel cell systems characterised by the implementation of mathematical or computational algorithms, e.g. feedback control loops, fuzzy logic, neural networks or artificial intelligence
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
Landscapes
- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Electrochemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Chemical & Material Sciences (AREA)
- Sustainable Energy (AREA)
- Sustainable Development (AREA)
- Manufacturing & Machinery (AREA)
- Computing Systems (AREA)
- Theoretical Computer Science (AREA)
- Software Systems (AREA)
- Medical Informatics (AREA)
- Fuzzy Systems (AREA)
- Evolutionary Computation (AREA)
- Health & Medical Sciences (AREA)
- Automation & Control Theory (AREA)
- Artificial Intelligence (AREA)
- Fuel Cell (AREA)
Abstract
本发明公开了一种燃料电池系统的局部电压检测装置及其检测分析方法,燃料电池系统包括控制器和划分若干个反应区域的燃料电池堆,局部电压检测装置包括用于检测若干个反应区域的局部电压信息的若干个电压感应探头和用于转换该局部电压信息后传输至控制器的电压采集模块;该方法包括:步骤1、获取燃料电池堆在不同电流下运行产生的若干组第一局部瞬时电压,判断燃料电池堆是否反应不均匀;若是,执行步骤2;若否,执行步骤1;步骤2、获取燃料电池堆在若干个变量参数逐个发生变化时运行产生的若干组第二局部瞬时电压,从中筛选整体数值相对较大的一组第二局部瞬时电压,获取其对应的变量参数。本发明可为技术人员调整电堆控制策略提供参考依据。
The invention discloses a local voltage detection device of a fuel cell system and a detection and analysis method thereof. The fuel cell system includes a controller and a fuel cell stack divided into several reaction areas. The local voltage detection device includes a device for detecting several reaction areas. Several voltage sensing probes for local voltage information and a voltage acquisition module for converting the local voltage information and transmitting it to the controller; the method includes: step 1. Obtaining several groups of first partial signals generated by the fuel cell stack operating under different currents. Instantaneous voltage to determine whether the fuel cell stack reacts unevenly; if so, perform step 2; if not, perform step 1; step 2, obtain several sets of second partial instantaneous results generated by the operation of the fuel cell stack when several variable parameters change one by one. voltage, from which a group of second partial instantaneous voltages with relatively large overall values are screened, and their corresponding variable parameters are obtained. The present invention can provide a reference basis for technicians to adjust the stack control strategy.
Description
技术领域Technical field
本发明涉及燃料电池应用技术领域,具体是涉及一种燃料电池系统的局部电压检测装置及其检测分析方法。The invention relates to the technical field of fuel cell applications, and in particular to a local voltage detection device of a fuel cell system and a detection and analysis method thereof.
背景技术Background technique
燃料电池堆在工作时的内部环境十分复杂,受到气体分布均匀性、温度等因素的影响,燃料电池堆的相邻区域形成电压差异,产生局部电流,影响电堆性能,严重时甚至导致质子交换膜穿孔,损坏电堆。然而,目前的燃料电池系统并未提出对燃料电池堆进行分区域的局部电流检测,进而未能分析产生局部电压差异的因素,无法采取相应的控制措施来确保燃料电池堆内部反应均匀。The internal environment of the fuel cell stack is very complex when it is working. Affected by factors such as gas distribution uniformity and temperature, adjacent areas of the fuel cell stack form voltage differences, generate local currents, affect the performance of the stack, and even lead to proton exchange in severe cases. The membrane is perforated and the stack is damaged. However, the current fuel cell system does not propose local current detection of the fuel cell stack in different regions, and thus fails to analyze the factors causing local voltage differences and cannot take corresponding control measures to ensure uniform reactions within the fuel cell stack.
发明内容Contents of the invention
本发明提供一种燃料电池系统的局部电压检测装置及其检测分析方法,以解决现有技术中所存在的一个或多个技术问题,至少提供一种有益的选择或创造条件。The present invention provides a local voltage detection device of a fuel cell system and a detection and analysis method thereof to solve one or more technical problems existing in the prior art and at least provide a beneficial choice or creation condition.
本发明实施例提供一种燃料电池系统的局部电压检测装置,所述燃料电池系统包括燃料电池堆和控制器,所述局部电压检测装置包括若干个电压感应探头和电压采集模块,所述若干个电压感应探头与所述电压采集模块连接,所述电压采集模块与所述控制器连接;Embodiments of the present invention provide a local voltage detection device of a fuel cell system. The fuel cell system includes a fuel cell stack and a controller. The local voltage detection device includes a plurality of voltage sensing probes and voltage acquisition modules. The plurality of The voltage sensing probe is connected to the voltage acquisition module, and the voltage acquisition module is connected to the controller;
所述燃料电池堆上均匀划分出若干个反应区域,所述若干个电压感应探头对应设置在所述若干个反应区域,其中任意一个电压感应探头用于检测其所在反应区域内的局部电压信息,所述电压采集模块用于将所述局部电压信息转换为所述控制器可识别的局部电压信号并将其传输至所述控制器。Several reaction areas are evenly divided on the fuel cell stack, and the plurality of voltage sensing probes are correspondingly arranged in the several reaction areas, and any one of the voltage sensing probes is used to detect local voltage information in the reaction area where it is located, The voltage acquisition module is used to convert the local voltage information into a local voltage signal identifiable by the controller and transmit it to the controller.
进一步地,所述燃料电池系统还包括氢气供应模块、空气供应模块和热能管理模块;Further, the fuel cell system also includes a hydrogen supply module, an air supply module and a thermal energy management module;
所述氢气供应模块与所述燃料电池堆连接,且所述氢气供应模块受控于所述控制器,用于向所述燃料电池堆输送实际所需的氢气;The hydrogen supply module is connected to the fuel cell stack, and the hydrogen supply module is controlled by the controller for delivering the actual required hydrogen to the fuel cell stack;
所述空气供应模块与所述燃料电池堆连接,且所述空气供应模块受控于所述控制器,用于向所述燃料电池堆输送实际所需的空气;The air supply module is connected to the fuel cell stack, and the air supply module is controlled by the controller for delivering actual required air to the fuel cell stack;
所述热能管理模块与所述燃料电池堆连接,且所述热能管理模块受控于所述控制器,用于对所述燃料电池堆的出入口进行散热调控。The thermal energy management module is connected to the fuel cell stack, and is controlled by the controller for regulating heat dissipation at the entrance and exit of the fuel cell stack.
另外,本发明实施例还提供一种燃料电池系统局部电压检测装置的检测分析方法,应用上述任一项所述的燃料电池系统的局部电压检测装置,所述检测分析方法包括:In addition, embodiments of the present invention also provide a detection and analysis method for a local voltage detection device of a fuel cell system, using any of the above-mentioned local voltage detection devices of the fuel cell system. The detection and analysis method includes:
步骤S100、获取影响燃料电池堆运行的若干个变量参数;Step S100: Obtain several variable parameters that affect the operation of the fuel cell stack;
步骤S200、获取所述燃料电池堆在不同电流下运行所产生的若干组第一局部瞬时电压,再将所述燃料电池堆的工作电流调节至初始状态;Step S200: Obtain several sets of first local instantaneous voltages generated by the fuel cell stack operating under different currents, and then adjust the operating current of the fuel cell stack to the initial state;
步骤S300、利用所述若干组第一局部瞬时电压判断所述燃料电池堆是否发生反应不均匀的现象;若是,继续执行步骤S400;若否,返回执行步骤S200;Step S300: Use the plurality of sets of first local instantaneous voltages to determine whether uneven reaction occurs in the fuel cell stack; if yes, continue to step S400; if not, return to step S200;
步骤S400、获取所述燃料电池堆在所述若干个变量参数逐个单独发生变化时运行所产生的若干组第二局部瞬时电压,并且所述若干组第二局部瞬时电压是在相同指定电流下采集得到的;Step S400: Obtain several sets of second local instantaneous voltages generated by the operation of the fuel cell stack when the several variable parameters change individually, and the sets of second local instantaneous voltages are collected at the same specified current. owned;
步骤S500、从所述若干组第二局部瞬时电压中筛选出整体数值相对较大的一组第二局部瞬时电压,再将该组第二局部瞬时电压所对应的变量参数指定为对所述燃料电池堆当前运行状态影响最大的一个变量参数。Step S500: Select a group of second local instantaneous voltages with a relatively large overall value from the plurality of groups of second local instantaneous voltages, and then specify the variable parameters corresponding to the group of second local instantaneous voltages as the values for the fuel. The variable parameter that has the greatest impact on the current operating status of the battery stack.
进一步地,所述步骤S200的实施过程包括:Further, the implementation process of step S200 includes:
步骤S210、当所述燃料电池堆的工作电流保持为I0时,控制所述燃料电池堆稳定运行一段时间,其中I0表示为电流初始状态;Step S210: When the operating current of the fuel cell stack remains I 0 , control the fuel cell stack to operate stably for a period of time, where I 0 represents the initial state of the current;
步骤S220、当所述燃料电池堆的工作电流增加至I0+k×ΔI时,获取所述燃料电池堆运行所产生的第k组第一局部瞬时电压,其中ΔI为设定的电流增值;Step S220: When the operating current of the fuel cell stack increases to I 0 +k×ΔI, obtain the kth group of first local instantaneous voltages generated by the operation of the fuel cell stack, where ΔI is the set current increment;
步骤S230、判断k≥N1是否成立,其中N1为设定的采集总次数,N1为正整数且N1≥2;若成立,则继续执行步骤S240;若不成立,则控制所述燃料电池堆稳定运行一段时间之后,将k+1赋值给k,返回执行步骤S220;Step S230, determine whether k≥N 1 is established, where N 1 is the set total number of collections, N 1 is a positive integer and N 1 ≥ 2; if it is established, continue to execute step S240; if it is not established, control the fuel After the battery stack has been running stably for a period of time, k+1 is assigned to k and returns to step S220;
步骤S240、输出N1组第一局部瞬时电压,再将所述燃料电池堆的工作电流调节至初始状态;Step S240: Output N 1 sets of first local instantaneous voltages, and then adjust the operating current of the fuel cell stack to the initial state;
其中,上述步骤S220和上述步骤S230形成循环操作,且该循环操作从k=1开始执行。Among them, the above-mentioned step S220 and the above-mentioned step S230 form a loop operation, and the loop operation is executed starting from k=1.
进一步地,所述步骤S300的实施过程为:Further, the implementation process of step S300 is:
从所述N1组第一局部瞬时电压中筛选出整体数值不完全相同的M组第一局部瞬时电压,判断M是否小于既定阈值;若是,则判断所述燃料电池堆内部反应均匀;若否,则判断所述燃料电池堆内部反应不均匀。Screen out M groups of first local instantaneous voltages whose overall values are not exactly the same from the N 1 groups of first local instantaneous voltages, and determine whether M is less than the established threshold; if so, determine that the internal reaction of the fuel cell stack is uniform; if not , then it is judged that the internal reaction of the fuel cell stack is uneven.
进一步地,所述若干个变量参数包括空气流量和氢气流量,所述空气流量与过量空气系数相关联,所述氢气流量与氢气过量系数相关联。Further, the several variable parameters include air flow and hydrogen flow, the air flow is associated with the excess air coefficient, and the hydrogen flow is associated with the hydrogen excess coefficient.
进一步地,所述步骤S400的实施过程包括:Further, the implementation process of step S400 includes:
步骤S410、当所述燃料电池堆的工作电流保持为I0时,控制所述燃料电池堆稳定运行一段时间,其中I0表示为电流初始状态;Step S410: When the operating current of the fuel cell stack remains at I 0 , control the fuel cell stack to operate stably for a period of time, where I 0 represents the initial state of the current;
步骤S420、将所述过量空气系数由初始值λ1提高至λ1+Δλ1,控制所述燃料电池堆稳定运行一段时间之后,将所述燃料电池堆的工作电流增加至I0+ΔI,获取所述燃料电池堆运行所产生的第一组第二局部瞬时电压,其中Δλ1为设定的第一系数增值,ΔI为设定的电流增值;Step S420: Increase the excess air coefficient from the initial value λ 1 to λ 1 +Δλ 1 , and after controlling the fuel cell stack to operate stably for a period of time, increase the operating current of the fuel cell stack to I 0 +ΔI, Obtain the first set of second local instantaneous voltages generated by the operation of the fuel cell stack, where Δλ 1 is the set first coefficient increment, and ΔI is the set current increment;
步骤S430、当所述燃料电池堆的工作电流从I0+ΔI恢复至I0并且所述过量空气系数从λ1+Δλ1恢复至λ1时,控制所述燃料电池堆稳定运行一段时间;Step S430: When the operating current of the fuel cell stack recovers from I 0 +ΔI to I 0 and the excess air coefficient recovers from λ 1 +Δλ 1 to λ 1 , control the fuel cell stack to operate stably for a period of time;
步骤S440、将所述氢气过量系数由初始值λ2提高至λ2+Δλ2,控制所述燃料电池堆稳定运行一段时间之后,将所述燃料电池堆的工作电流增加至I0+ΔI,获取所述燃料电池堆运行所产生的第二组第二局部瞬时电压,其中Δλ2为设定的第二系数增值;Step S440: Increase the hydrogen excess coefficient from the initial value λ 2 to λ 2 +Δλ 2 , and after controlling the fuel cell stack to operate stably for a period of time, increase the operating current of the fuel cell stack to I 0 +ΔI, Obtain a second set of second local instantaneous voltages generated by the operation of the fuel cell stack, where Δλ 2 is the set second coefficient increment;
步骤S450、将所述燃料电池堆的工作电流从I0+ΔI恢复至I0,以及将所述过量空气系数从λ1+Δλ1恢复至λ1。Step S450: Restoring the operating current of the fuel cell stack from I 0 +ΔI to I 0 , and restoring the excess air coefficient from λ 1 +Δλ 1 to λ 1 .
进一步地,所述步骤S500的实施过程包括:Further, the implementation process of step S500 includes:
当所述第一组第二局部瞬时电压的整体数值大于所述第二组第二局部瞬时电压的整体数值时,将所述第一组第二局部瞬时电压所对应的空气流量指定为对所述燃料电池堆当前运行状态影响最大的一个变量参数;When the overall value of the first group of second local instantaneous voltages is greater than the overall value of the second group of second local instantaneous voltages, the air flow corresponding to the first group of second local instantaneous voltages is designated as the air flow rate corresponding to the first group of second local instantaneous voltages. The variable parameter that has the greatest influence on the current operating status of the fuel cell stack is described below;
或者,当所述第二组第二局部瞬时电压的整体数值大于所述第一组第二局部瞬时电压的整体数值时,将所述第二组第二局部瞬时电压所对应的氢气流量指定为对所述燃料电池堆当前运行状态影响最大的一个变量参数。Alternatively, when the overall value of the second group of second local instantaneous voltages is greater than the overall value of the first group of second local instantaneous voltages, the hydrogen flow rate corresponding to the second group of second local instantaneous voltages is designated as A variable parameter that has the greatest influence on the current operating state of the fuel cell stack.
本发明至少具有以下有益效果:通过将燃料电池堆均匀划分出若干个反应区域,并利用若干个电压感应探头对其进行测量,可以保证采集到的每个反应区域的瞬时电压是同一时刻的,由此确保后续执行电压分析任务时的数据可靠性。通过采集燃料电池堆的若干个反应区域在不同电流下运行所产生的瞬时电压并对其进行分析,可以更为准确地获知燃料电池堆的内部反应情况。通过采集燃料电池堆的若干个反应区域在不同变量参数发生变化时运行所产生的瞬时电压并对其进行对比分析,可以更为准确地获取对燃料电池堆影响最大的变量参数,以便于技术人员及时调整对燃料电池堆的运行控制策略,进一步提高燃料电池系统的运行效率。The present invention at least has the following beneficial effects: by evenly dividing the fuel cell stack into several reaction areas and using several voltage sensing probes to measure them, it can ensure that the instantaneous voltage of each reaction area collected is at the same time. This ensures data reliability when performing subsequent voltage analysis tasks. By collecting and analyzing the instantaneous voltages generated by several reaction areas of the fuel cell stack operating at different currents, the internal reaction conditions of the fuel cell stack can be obtained more accurately. By collecting the instantaneous voltages generated by the operation of several reaction areas of the fuel cell stack when different variable parameters change and conducting comparative analysis on them, the variable parameters that have the greatest impact on the fuel cell stack can be more accurately obtained to facilitate technicians Timely adjust the operation control strategy of the fuel cell stack to further improve the operating efficiency of the fuel cell system.
附图说明Description of the drawings
附图用来提供对本发明技术方案的进一步理解,并且构成说明书的一部分,与本发明的实施例一起用于解释本发明的技术方案,并不构成对本发明技术方案的限制。The accompanying drawings are used to provide a further understanding of the technical solutions of the present invention, and constitute a part of the description. Together with the embodiments of the present invention, they are used to explain the technical solutions of the present invention, and do not constitute a limitation of the technical solutions of the present invention.
图1是本发明实施例中的一种燃料电池系统的局部电压检测装置的结构组成示意图;Figure 1 is a schematic structural diagram of a local voltage detection device of a fuel cell system in an embodiment of the present invention;
图2是本发明实施例中的若干个电压感应探头设置在燃料电池堆上的安装分布示意图;Figure 2 is a schematic diagram of the installation distribution of several voltage sensing probes arranged on the fuel cell stack in the embodiment of the present invention;
图3是本发明实施例中的一种燃料电池系统局部电压检测装置的检测分析方法的流程示意图。Figure 3 is a schematic flowchart of a detection and analysis method of a local voltage detection device of a fuel cell system in an embodiment of the present invention.
具体实施方式Detailed ways
为了使本发明的目的、技术方案及优点更加清楚明白,以下结合附图及实施例对本发明进行进一步详细说明。应当理解,此处所描述的具体实施例仅用以解释本发明,并不用于限定本发明。In order to make the purpose, technical solutions and advantages of the present invention more clear, the present invention will be further described in detail below with reference to the accompanying drawings and embodiments. It should be understood that the specific embodiments described here are only used to explain the present invention and are not intended to limit the present invention.
需要说明的是,虽然在系统示意图中进行了功能模块划分,在流程图中示出了逻辑顺序,但是在某些情况下,可以以不同于系统中的模块划分,或流程图中的顺序执行所示出或描述的步骤。说明书和权利要求书及上述附图中的术语“第一”、“第二”等是用于区别类似的对象,而不必用于描述特定的顺序或先后次序。It should be noted that although the functional modules are divided in the system schematic diagram and the logical sequence is shown in the flow chart, in some cases, the modules can be divided into different modules in the system or the order in the flow chart can be executed. The steps shown or described. The terms "first", "second", etc. in the description, claims, and above-mentioned drawings are used to distinguish similar objects and are not necessarily used to describe a specific sequence or sequence.
请参考图1至图2,本发明实施例提供一种燃料电池系统的局部电压检测装置,其中所述燃料电池系统包括燃料电池堆、控制器、氢气供应模块、空气供应模块和热能管理模块,所述局部电压检测装置包括若干个电压感应探头和电压采集模块,在所述燃料电池堆上均匀划分出若干个反应区域(在图2中表示为区域1至区域2N),所述若干个电压感应探头(在图2中表示为电压感应探头1至电压感应探头2N)对应设置在所述若干个反应区域,即确保每一个反应区域配备有一个电压感应探头进行检测。Please refer to Figures 1 to 2. An embodiment of the present invention provides a local voltage detection device for a fuel cell system, wherein the fuel cell system includes a fuel cell stack, a controller, a hydrogen supply module, an air supply module and a thermal energy management module. The local voltage detection device includes several voltage sensing probes and voltage acquisition modules, and several reaction areas (represented as area 1 to area 2N in Figure 2) are evenly divided on the fuel cell stack. The sensing probes (represented as voltage sensing probe 1 to voltage sensing probe 2N in Figure 2) are correspondingly arranged in the several reaction areas, that is, ensuring that each reaction area is equipped with a voltage sensing probe for detection.
在本发明实施例中,所述氢气供应模块与所述燃料电池堆连接,且所述氢气供应模块受控于所述控制器,用于向所述燃料电池堆输送实际所需的氢气;所述空气供应模块与所述燃料电池堆连接,且所述空气供应模块受控于所述控制器,用于向所述燃料电池堆输送实际所需的空气;所述热能管理模块与所述燃料电池堆连接,且所述热能管理模块受控于所述控制器,用于对所述燃料电池堆的出入口进行散热调控以及时排出所述燃料电池堆所产生的多余热量;所述若干个电压感应探头与所述电压采集模块连接,所述电压采集模块与所述控制器连接,其中任意一个电压感应探头用于检测其所在反应区域内的局部电压信息,所述电压采集模块用于将所述局部电压信息转换为所述控制器可识别的局部电压信号并将其传输至所述控制器以执行后续的瞬时电压分析任务。In an embodiment of the present invention, the hydrogen supply module is connected to the fuel cell stack, and the hydrogen supply module is controlled by the controller for delivering the actual required hydrogen to the fuel cell stack; The air supply module is connected to the fuel cell stack, and the air supply module is controlled by the controller to deliver actual required air to the fuel cell stack; the thermal energy management module is connected to the fuel cell stack. The battery stack is connected, and the thermal energy management module is controlled by the controller, which is used to regulate heat dissipation at the entrance and exit of the fuel cell stack and discharge excess heat generated by the fuel cell stack in a timely manner; the plurality of voltages The induction probe is connected to the voltage acquisition module, and the voltage acquisition module is connected to the controller. Any one of the voltage induction probes is used to detect the local voltage information in the reaction area where it is located, and the voltage acquisition module is used to collect all the voltage information. The local voltage information is converted into a local voltage signal identifiable by the controller and transmitted to the controller to perform subsequent instantaneous voltage analysis tasks.
具体的,所述控制器可以用于调控所述氢气供应模块向所述燃料电池堆所输送的氢气的流量、温度和湿度,还可以用于调控所述空气供应模块向所述燃料电池堆所输送的空气的流量、温度和湿度,以及用于调控所述热能管理模块对所述燃料电池堆的入口温度和出口温度的散热程度。Specifically, the controller can be used to regulate the flow rate, temperature and humidity of hydrogen delivered by the hydrogen supply module to the fuel cell stack, and can also be used to regulate the flow of hydrogen delivered by the air supply module to the fuel cell stack. The flow rate, temperature and humidity of the delivered air, and the degree of heat dissipation used to regulate the inlet temperature and outlet temperature of the fuel cell stack by the thermal energy management module.
其中,所述氢气供应模块包括氢气供应设备、第一入口阀、第一排气阀和氢气循环泵,所述空气供应模块包括空气供应设备、第二入口阀和第二排气阀,所述热能管理模块包括散热器和冷却液循环泵,上述三个模块均为现有燃料电池系统中的常用设备,不属于本发明所要保护的内容,在此不再进行赘述。Wherein, the hydrogen supply module includes a hydrogen supply device, a first inlet valve, a first exhaust valve and a hydrogen circulation pump; the air supply module includes an air supply device, a second inlet valve and a second exhaust valve; The thermal energy management module includes a radiator and a coolant circulation pump. The above three modules are all common equipment in existing fuel cell systems and do not belong to the content to be protected by the present invention, so they will not be described again here.
基于上述提及到的所述燃料电池系统的局部电压检测装置,本发明实施例还提供一种燃料电池系统局部电压检测装置的检测分析方法,参见图3所示出的流程示意图,所述检测分析方法包括如下:Based on the above-mentioned local voltage detection device of the fuel cell system, an embodiment of the present invention also provides a detection and analysis method of the local voltage detection device of the fuel cell system. Refer to the schematic flow chart shown in Figure 3. The detection method Analysis methods include the following:
步骤S100、获取影响燃料电池堆运行的若干个变量参数;Step S100: Obtain several variable parameters that affect the operation of the fuel cell stack;
步骤S200、获取所述燃料电池堆在不同电流下运行所产生的若干组第一局部瞬时电压,再将所述燃料电池堆的工作电流调节至初始状态;Step S200: Obtain several sets of first local instantaneous voltages generated by the fuel cell stack operating under different currents, and then adjust the operating current of the fuel cell stack to the initial state;
步骤S300、利用所述若干组第一局部瞬时电压判断所述燃料电池堆是否发生反应不均匀的现象;若是,继续执行步骤S400;若否,返回执行步骤S200;Step S300: Use the plurality of sets of first local instantaneous voltages to determine whether uneven reaction occurs in the fuel cell stack; if yes, continue to step S400; if not, return to step S200;
步骤S400、获取所述燃料电池堆在所述若干个变量参数逐个单独发生变化时运行所产生的若干组第二局部瞬时电压,并且所述若干组第二局部瞬时电压是在相同指定电流下采集得到的;Step S400: Obtain several sets of second local instantaneous voltages generated by the operation of the fuel cell stack when the several variable parameters change individually, and the sets of second local instantaneous voltages are collected at the same specified current. owned;
步骤S500、从所述若干组第二局部瞬时电压中筛选出整体数值相对较大的一组第二局部瞬时电压,再将该组第二局部瞬时电压所对应的变量参数指定为对所述燃料电池堆当前运行状态影响最大的一个变量参数。Step S500: Select a group of second local instantaneous voltages with a relatively large overall value from the plurality of groups of second local instantaneous voltages, and then specify the variable parameters corresponding to the group of second local instantaneous voltages as the values for the fuel. The variable parameter that has the greatest impact on the current operating status of the battery stack.
在上述步骤S200中,任意一组第一局部瞬时电压是由所述若干个电压感应探头所检测到的,也就是说,任意一组第一局部瞬时电压所包含的第一瞬时电压的数量与所述若干个电压感应探头的数量相同。In the above step S200, any group of first local instantaneous voltages is detected by the plurality of voltage sensing probes, that is to say, the number of first instantaneous voltages included in any group of first local instantaneous voltages The same number as the number of voltage sensing probes.
在上述步骤S400中,任意一组第二局部瞬时电压是由所述若干个电压感应探头所检测到的;所述若干组第二局部瞬时电压的组数与所述若干个变量参数的数量相同,当所述若干个变量参数的数量为K时,任意一组第二局部瞬时电压是在K-1个变量参数保持不变、仅一个变量参数发生变化的情况下采集得到的,且每一组第二局部瞬时电压所针对的发生变化的变量参数互不相同。In the above step S400, any set of second local instantaneous voltages is detected by the plurality of voltage sensing probes; the number of sets of second local instantaneous voltages is the same as the number of the plurality of variable parameters. , when the number of the several variable parameters is K, any set of second local instantaneous voltages is collected under the condition that K-1 variable parameters remain unchanged and only one variable parameter changes, and each The variable parameters for which the second local instantaneous voltages of the group change are different from each other.
在本发明实施例中,所述步骤S200的实施过程包括如下:In the embodiment of the present invention, the implementation process of step S200 includes the following:
步骤S210、当所述燃料电池堆的工作电流保持为I0时,控制所述燃料电池堆稳定运行一段时间,其中I0表示为电流初始状态;Step S210: When the operating current of the fuel cell stack remains I 0 , control the fuel cell stack to operate stably for a period of time, where I 0 represents the initial state of the current;
步骤S220、当所述燃料电池堆的工作电流增加至I0+k×ΔI时,获取所述燃料电池堆运行所产生的第k组第一局部瞬时电压,其中ΔI为设定的电流增值;Step S220: When the operating current of the fuel cell stack increases to I 0 +k×ΔI, obtain the kth group of first local instantaneous voltages generated by the operation of the fuel cell stack, where ΔI is the set current increment;
步骤S230、判断k≥N1是否成立,其中N1为设定的采集总次数,N1为正整数且N1≥2;若成立,则继续执行步骤S240;若不成立,则控制所述燃料电池堆稳定运行一段时间之后,将k+1赋值给k,返回执行步骤S220;Step S230, determine whether k≥N 1 is established, where N 1 is the set total number of collections, N 1 is a positive integer and N 1 ≥ 2; if it is established, continue to execute step S240; if it is not established, control the fuel After the battery stack has been running stably for a period of time, k+1 is assigned to k and returns to step S220;
步骤240、输出N1组第一局部瞬时电压,再将所述燃料电池堆的工作电流调节至初始状态,即使得所述燃料电池堆的工作电流保持为I0;Step 240: Output the first local instantaneous voltage of the N 1 group, and then adjust the operating current of the fuel cell stack to the initial state, that is, the operating current of the fuel cell stack is maintained at I 0 ;
其中,上述步骤S220和上述步骤S230形成循环操作,且该循环操作从k=1开始执行,由此确保该循环操作可执行N1次以获取到N1组第一局部瞬时电压。The above-mentioned step S220 and the above-mentioned step S230 form a loop operation, and the loop operation is executed starting from k=1, thereby ensuring that the loop operation can be executed N 1 times to obtain N 1 sets of first local instantaneous voltages.
在本发明实施例中,所述步骤S300的实施过程为:从所述N1组第一局部瞬时电压中筛选出整体数值不完全相同的M组第一局部瞬时电压,判断M是否小于既定阈值;若是,则判断所述燃料电池堆内部反应均匀;若否,则判断所述燃料电池堆内部反应不均匀。In the embodiment of the present invention, the implementation process of step S300 is: filter out M groups of first local instantaneous voltages whose overall values are not exactly the same from the N 1 groups of first local instantaneous voltages, and determine whether M is less than a predetermined threshold. ; If yes, it is determined that the internal reaction of the fuel cell stack is uniform; if not, then it is determined that the internal reaction of the fuel cell stack is uneven.
其中,所述既定阈值视N1的取值而定,以确保所述N1组第一局部瞬时电压中存在绝大多组第一局部瞬时电压处于整体数值完全相同的状态,也就是说,所述绝大多组第一局部瞬时电压中的任意一组第一局部瞬时电压内所包含的所有第一局部瞬时电压的数值相同,此时可以判断在采集该组第一局部瞬时电压时,所述燃料电池堆的内部反应均匀。The predetermined threshold depends on the value of N 1 to ensure that among the N 1 groups of first local instantaneous voltages, most groups of first local instantaneous voltages are in a state with exactly the same overall value. That is to say, all All the first local instantaneous voltages contained in any group of first local instantaneous voltages among the majority of the first partial instantaneous voltages have the same value. At this time, it can be judged that when collecting the first partial instantaneous voltages of the group, the The internal reactions of the fuel cell stack are uniform.
需要说明的是,在上述步骤S200中,当该循环操作执行至将所述燃料电池堆的工作电流增加至I0+N1×ΔI时,该工作电流I0+N1×ΔI不应当超过所述燃料电池堆的允许工作电流范围,以避免对所述燃料电池堆造成不必要的损坏;除此之外,上述步骤S300提出利用所述N1组第一局部瞬时电压进行反应不均匀判断,可以避免因偶然性事件造成误判。It should be noted that in the above step S200, when the cyclic operation is performed to increase the operating current of the fuel cell stack to I 0 +N 1 ×ΔI, the operating current I 0 +N 1 ×ΔI should not exceed The allowable operating current range of the fuel cell stack is to avoid unnecessary damage to the fuel cell stack; in addition, the above-mentioned step S300 proposes to use the first local instantaneous voltage of the N 1 group to determine the reaction unevenness , which can avoid misjudgments caused by accidental events.
在本发明实施例中,所述若干个变量参数包括但不仅限于空气流量和氢气流量;其中,所述空气流量与过量空气系数相关联,所述氢气流量与氢气过量系数相关联,它们之间的关联性属于现有技术,在此不再进行赘述。In the embodiment of the present invention, the several variable parameters include but are not limited to air flow and hydrogen flow; wherein, the air flow is associated with the excess air coefficient, the hydrogen flow is associated with the hydrogen excess coefficient, and between them The correlation belongs to the existing technology and will not be described again here.
在本发明实施例中,所述步骤S400的实施过程包括:In this embodiment of the present invention, the implementation process of step S400 includes:
步骤S410、当所述燃料电池堆的工作电流保持为I0时,控制所述燃料电池堆稳定运行一段时间,其中I0表示为电流初始状态;Step S410: When the operating current of the fuel cell stack remains at I 0 , control the fuel cell stack to operate stably for a period of time, where I 0 represents the initial state of the current;
步骤S420、将所述过量空气系数由初始值λ1提高至λ1+Δλ1,控制所述燃料电池堆稳定运行一段时间之后,将所述燃料电池堆的工作电流增加至I0+ΔI,获取所述燃料电池堆运行所产生的第一组第二局部瞬时电压,其中Δλ1为设定的第一系数增值,ΔI为设定的电流增值;Step S420: Increase the excess air coefficient from the initial value λ 1 to λ 1 +Δλ 1 , and after controlling the fuel cell stack to operate stably for a period of time, increase the operating current of the fuel cell stack to I 0 +ΔI, Obtain the first set of second local instantaneous voltages generated by the operation of the fuel cell stack, where Δλ 1 is the set first coefficient increment, and ΔI is the set current increment;
步骤S430、当所述燃料电池堆的工作电流从I0+ΔI恢复至I0并且所述过量空气系数从λ1+Δλ1恢复至λ1时,控制所述燃料电池堆稳定运行一段时间;Step S430: When the operating current of the fuel cell stack recovers from I 0 +ΔI to I 0 and the excess air coefficient recovers from λ 1 +Δλ 1 to λ 1 , control the fuel cell stack to operate stably for a period of time;
步骤S440、将所述氢气过量系数由初始值λ2提高至λ2+Δλ2,控制所述燃料电池堆稳定运行一段时间之后,将所述燃料电池堆的工作电流增加至I0+ΔI,获取所述燃料电池堆运行所产生的第二组第二局部瞬时电压,其中Δλ2为设定的第二系数增值;Step S440: Increase the hydrogen excess coefficient from the initial value λ 2 to λ 2 +Δλ 2 , and after controlling the fuel cell stack to operate stably for a period of time, increase the operating current of the fuel cell stack to I 0 +ΔI, Obtain a second set of second local instantaneous voltages generated by the operation of the fuel cell stack, where Δλ 2 is the set second coefficient increment;
步骤S450、将所述燃料电池堆的工作电流从I0+ΔI恢复至I0,以及将所述过量空气系数从λ1+Δλ1恢复至λ1。Step S450: Restoring the operating current of the fuel cell stack from I 0 +ΔI to I 0 , and restoring the excess air coefficient from λ 1 +Δλ 1 to λ 1 .
在本发明实施例中,所述步骤S500的实施过程包括:当所述第一组第二局部瞬时电压的整体数值大于所述第二组第二局部瞬时电压的整体数值时,将所述第一组第二局部瞬时电压所对应的空气流量指定为对所述燃料电池堆当前运行状态影响最大的一个变量参数;或者,当所述第二组第二局部瞬时电压的整体数值大于所述第一组第二局部瞬时电压的整体数值时,将所述第二组第二局部瞬时电压所对应的氢气流量指定为对所述燃料电池堆当前运行状态影响最大的一个变量参数。In the embodiment of the present invention, the implementation process of step S500 includes: when the overall value of the first group of second local instantaneous voltages is greater than the overall value of the second group of second local instantaneous voltages, The air flow corresponding to a set of second local instantaneous voltages is designated as a variable parameter that has the greatest influence on the current operating state of the fuel cell stack; or, when the overall value of the second set of second local instantaneous voltages is greater than the first When the overall value of a set of second local instantaneous voltages is determined, the hydrogen flow rate corresponding to the second set of second local instantaneous voltages is designated as a variable parameter that has the greatest influence on the current operating state of the fuel cell stack.
在一般情况下,所述第一组第二局部瞬时电压的整体数值和所述第二组第二局部瞬时电压的整体数值并不会存在完全相同的情况,若有例外,则同时将空气流量和氢气流量均指定为对所述燃料电池堆当前运行状态影响较大的两个变量参数。Under normal circumstances, the overall value of the first group of second local instantaneous voltages and the overall value of the second group of second local instantaneous voltages will not be exactly the same. If there are exceptions, the air flow rate will be changed at the same time. and hydrogen flow rate are designated as two variable parameters that have a greater impact on the current operating status of the fuel cell stack.
需要说明的是,在上述步骤S200和步骤S400中所提及到的控制所述燃料电池堆稳定运行一段时间,其实施效果表现为:所述若干个电压感应探头所检测到的若干个电压数据可以保持在稳定状态。It should be noted that the implementation effect of controlling the fuel cell stack to operate stably for a period of time as mentioned in the above steps S200 and S400 is as follows: several voltage data detected by the several voltage sensing probes can be maintained in a stable state.
需要说明的是,上述步骤S300和步骤S500的分析过程是在所述控制器内执行的,而上述步骤S200中所涉及到的工作电流调整以及上述步骤S400中所涉及到的变量参数和工作电流的调整是由所述控制器进行控制调节的。It should be noted that the analysis process of the above steps S300 and step S500 is executed in the controller, and the working current adjustment involved in the above step S200 and the variable parameters and working current involved in the above step S400 are The adjustment is controlled and adjusted by the controller.
在本发明实施例中,针对一个输出功率为5kW的燃料电池堆进行测量,以所述局部电压检测装置包括6个电压感应探头为例,对上述步骤S400和步骤S500的实施过程进行细化举例说明,具体包括如下:In the embodiment of the present invention, a fuel cell stack with an output power of 5kW is measured. Taking the local voltage detection device including 6 voltage sensing probes as an example, the implementation process of the above steps S400 and S500 is detailed and exemplified. Description, specifically including the following:
步骤A1、当该燃料电池堆的工作电流保持为1A时,控制该燃料电池堆稳定运行一段时间;Step A1: When the operating current of the fuel cell stack is maintained at 1A, control the fuel cell stack to operate stably for a period of time;
步骤A2、将过量空气系数由初始值1.1提高至1.5,控制该燃料电池堆稳定运行一段时间之后,将该燃料电池堆的工作电流增加至1.5A,获取该燃料电池堆运行产生的第一组第二局部瞬时电压为:U5,air=706mV,U6,air=704mV,U1,air=U2,air=U3,air=U4,air=707mV;Step A2: Increase the excess air coefficient from the initial value of 1.1 to 1.5. After controlling the fuel cell stack to operate stably for a period of time, increase the operating current of the fuel cell stack to 1.5A to obtain the first group of energy generated by the operation of the fuel cell stack. The second local instantaneous voltage is: U 5, air = 706mV, U 6, air = 704mV, U 1, air = U 2, air = U 3, air = U 4, air = 707mV;
步骤A3、当该燃料电池堆的工作电流从1.5A恢复至1A并且该过量空气系数从1.5恢复至1.1时,控制该燃料电池堆稳定运行一段时间;Step A3: When the operating current of the fuel cell stack returns from 1.5A to 1A and the excess air coefficient returns from 1.5 to 1.1, control the fuel cell stack to operate stably for a period of time;
步骤A4、将氢气过量系数由初始值1.1提高至1.5,控制该燃料电池堆稳定运行一段时间之后,将该燃料电池堆的工作电流增加至1.5A,获取该燃料电池堆运行产生的第二组第二局部瞬时电压为:U5,H2=705mV,U6,H2=702mV,U1,H2=U2,H2=U3,H2=U4,H2=707mV;Step A4: Increase the hydrogen excess coefficient from the initial value of 1.1 to 1.5. After controlling the fuel cell stack to operate stably for a period of time, increase the operating current of the fuel cell stack to 1.5A to obtain the second group of energy generated by the operation of the fuel cell stack. The second local instantaneous voltage is: U 5,H2 =705mV, U 6,H2 =702mV, U 1,H2 =U 2,H2 =U 3,H2 =U 4,H2 =707mV;
步骤A5、将该燃料电池堆的工作电流从1.5A恢复至1A,以及将该过量空气系数从1.5恢复至1.1;Step A5, restore the operating current of the fuel cell stack from 1.5A to 1A, and restore the excess air coefficient from 1.5 to 1.1;
步骤A6、通过对上述步骤A2所获取到的第一组第二局部瞬时电压和上述步骤A4所获取到的第二组第二局部瞬时电压进行对比可知,第一组第二局部瞬时电压的整体数值大于第二组第二局部瞬时电压的整体数值,则将空气流量指定为对该燃料电池堆当前运行状态影响最大的一个变量参数,由此告知技术人员可对当前空气流量进行调节以改善该燃料电池堆的运行状况。Step A6: By comparing the first set of second local instantaneous voltages obtained in the above step A2 and the second set of second local instantaneous voltages obtained in the above step A4, it can be seen that the overall value of the first set of second local instantaneous voltages is The value is greater than the overall value of the second group of second local instantaneous voltages, then the air flow is designated as the variable parameter that has the greatest impact on the current operating state of the fuel cell stack, thereby informing the technician that the current air flow can be adjusted to improve the The operating condition of the fuel cell stack.
在本发明实施例中,针对一个输出功率为10kW的燃料电池堆进行测量,以所述局部电压检测装置包括8个电压感应探头为例,对上述步骤S400和步骤S500的实施过程进行细化举例说明,具体包括如下:In the embodiment of the present invention, a fuel cell stack with an output power of 10kW is measured. Taking the local voltage detection device including 8 voltage sensing probes as an example, the implementation process of the above steps S400 and S500 is detailed and exemplified. Description, specifically including the following:
步骤B1、当该燃料电池堆的工作电流保持为2A时,控制该燃料电池堆稳定运行一段时间;Step B1: When the operating current of the fuel cell stack is maintained at 2A, control the fuel cell stack to operate stably for a period of time;
步骤B2、将过量空气系数由初始值1.1提高至1.2,控制该燃料电池堆稳定运行一段时间之后,将该燃料电池堆的工作电流增加至3A,获取该燃料电池堆运行产生的第一组第二局部瞬时电压为:U1,air=U2,air=708mV,U3,air=U4,air=U5,air=U6,air=710mV,U7,air=707mV,U8,air=709mV;Step B2: Increase the excess air coefficient from the initial value of 1.1 to 1.2. After controlling the fuel cell stack to operate stably for a period of time, increase the operating current of the fuel cell stack to 3A to obtain the first group of the fuel cell stack generated by the operation. The two local instantaneous voltages are: U 1, air = U 2, air = 708mV, U 3, air = U 4, air = U 5 , air = U 6 , air = 710mV, U 7, air = 707mV, U 8, air =709mV;
步骤B3、当该燃料电池堆的工作电流从3A恢复至2A并且该过量空气系数从1.2恢复至1.1时,控制该燃料电池堆稳定运行一段时间;Step B3: When the operating current of the fuel cell stack returns from 3A to 2A and the excess air coefficient returns from 1.2 to 1.1, control the fuel cell stack to operate stably for a period of time;
步骤B4、将氢气过量系数由初始值1.1提高至1.2,控制该燃料电池堆稳定运行一段时间之后,将该燃料电池堆的工作电流增加至3A,获取该燃料电池堆运行产生的第二组第二局部瞬时电压为:U1,H2=704mV,U2,H2=705mV,U3,H2=U4,H2=U5,H2=U6,H2=711mV,U7,H2=705mV,U8,H2=706mV;Step B4: Increase the hydrogen excess coefficient from the initial value 1.1 to 1.2. After controlling the fuel cell stack to operate stably for a period of time, increase the operating current of the fuel cell stack to 3A to obtain the second group of the fuel cell stack generated by the operation. The two local instantaneous voltages are: U 1,H2 =704mV, U 2,H2 =705mV, U 3,H2 =U 4,H2 =U 5,H2 =U 6,H2 =711mV, U 7,H2 =705mV, U 8,H2 =706mV;
步骤B5、将该燃料电池堆的工作电流从3A恢复至2A,以及将该过量空气系数从1.2恢复至1.1;Step B5, restore the operating current of the fuel cell stack from 3A to 2A, and restore the excess air coefficient from 1.2 to 1.1;
步骤B6、通过对上述步骤B2所获取到的第一组第二局部瞬时电压和上述步骤B4所获取到的第二组第二局部瞬时电压进行对比可知,第一组第二局部瞬时电压的整体数值大于第二组第二局部瞬时电压的整体数值,则将空气流量指定为对该燃料电池堆当前运行状态影响最大的一个变量参数,由此告知技术人员可对当前空气流量进行调节以改善该燃料电池堆的运行状况。Step B6: By comparing the first group of second local instantaneous voltages obtained in the above step B2 and the second group of second local instantaneous voltages obtained in the above step B4, it can be seen that the overall second group of the first group of second local instantaneous voltages is The value is greater than the overall value of the second group of second local instantaneous voltages, then the air flow is designated as the variable parameter that has the greatest impact on the current operating state of the fuel cell stack, thereby informing the technician that the current air flow can be adjusted to improve the The operating condition of the fuel cell stack.
尽管本申请的描述已经相当详尽且特别对几个所述实施例进行了描述,但其并非旨在局限于任何这些细节或实施例或任何特殊实施例,而是应当将其视作是通过参考所附权利要求,考虑到现有技术为这些权利要求提供广义的可能性解释,从而有效地涵盖本申请的预定范围。此外,上文以发明人可预见的实施例对本申请进行描述,其目的是为了提供有用的描述,而那些目前尚未预见的对本申请的非实质性改动仍可代表本申请的等效改动。Although the description of the present application has been quite thorough and has particularly described several of the described embodiments, it is not intended to be limited to any such details or embodiments or to any particular embodiment, but rather is to be considered by reference. The appended claims, taking into account the prior art, provide a broad possible interpretation of these claims to effectively cover the intended scope of the application. In addition, the above description of the present application is based on embodiments foreseeable by the inventor, with the purpose of providing a useful description, and those non-substantive changes to the present application that are not yet foreseeable can still represent equivalent changes to the present application.
Claims (7)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202210567954.5A CN114914492B (en) | 2022-05-24 | 2022-05-24 | Local voltage detection device of fuel cell system and detection analysis method thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202210567954.5A CN114914492B (en) | 2022-05-24 | 2022-05-24 | Local voltage detection device of fuel cell system and detection analysis method thereof |
Publications (2)
Publication Number | Publication Date |
---|---|
CN114914492A CN114914492A (en) | 2022-08-16 |
CN114914492B true CN114914492B (en) | 2023-10-31 |
Family
ID=82768528
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202210567954.5A Active CN114914492B (en) | 2022-05-24 | 2022-05-24 | Local voltage detection device of fuel cell system and detection analysis method thereof |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN114914492B (en) |
Citations (19)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6451463B1 (en) * | 1997-10-06 | 2002-09-17 | Reveo, Inc. | Electro-chemical power generation systems employing arrays of electronically-controllable discharging and/or recharging cells within a unity support structure |
CN1670647A (en) * | 2004-03-19 | 2005-09-21 | 上海神力科技有限公司 | Fuel Cell Controller Regional Bus Distributed Control System |
CN1680822A (en) * | 2004-04-07 | 2005-10-12 | 上海神力科技有限公司 | Voltage detecting monitor of large-scale integrated fuel battery |
CN1883072A (en) * | 2003-11-19 | 2006-12-20 | 日产自动车株式会社 | Fuel cell system |
JP2008177005A (en) * | 2007-01-18 | 2008-07-31 | Matsushita Electric Ind Co Ltd | Fuel cell system |
CN101351918A (en) * | 2005-12-27 | 2009-01-21 | 日产自动车株式会社 | Fuel cell system |
JP2009283138A (en) * | 2008-05-19 | 2009-12-03 | Honda Motor Co Ltd | Fuel cell system and its operation method |
CN102165637A (en) * | 2008-09-25 | 2011-08-24 | 丰田自动车株式会社 | Fuel cell system and method of detecting abnormality of fuel cell system |
CN102484265A (en) * | 2009-08-21 | 2012-05-30 | 丰田自动车株式会社 | Fuel cell system |
CN102646842A (en) * | 2011-02-22 | 2012-08-22 | 上海攀业氢能源科技有限公司 | Method for improving hydrogen utilization of fuel cell |
CN103293356A (en) * | 2012-02-29 | 2013-09-11 | 欧姆龙株式会社 | Voltage monitoring apparatus and method |
CN104282925A (en) * | 2013-07-11 | 2015-01-14 | 铃木株式会社 | Deterioration detection apparatus for vehicle-used fuel cell |
CN105446288A (en) * | 2015-04-16 | 2016-03-30 | 武汉众宇动力系统科技有限公司 | Fuel cell distributed control system and control method |
CN106374121A (en) * | 2015-07-21 | 2017-02-01 | 通用汽车环球科技运作有限责任公司 | Electrochemical hydrogen sensor for global/local hydrogen starvation detection in PEM fuel cells |
CN109301290A (en) * | 2018-11-23 | 2019-02-01 | 武汉理工大学 | A fuel cell voltage inspection system with flood diagnosis |
CN113193216A (en) * | 2021-04-25 | 2021-07-30 | 湖北工业大学 | Multi-stack fuel cell system independent of single-chip voltage inspection and control method |
EP3866320A1 (en) * | 2020-02-12 | 2021-08-18 | ABB Schweiz AG | Fuel cell power system |
CN113363539A (en) * | 2021-05-28 | 2021-09-07 | 电子科技大学 | High-resolution partition detection system for internal current of fuel cell stack |
CN113793952A (en) * | 2021-08-12 | 2021-12-14 | 上海电气集团股份有限公司 | Fuel cell system and low-temperature starting control method and device thereof |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP5168848B2 (en) * | 2006-08-10 | 2013-03-27 | 日産自動車株式会社 | Fuel cell system |
-
2022
- 2022-05-24 CN CN202210567954.5A patent/CN114914492B/en active Active
Patent Citations (19)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6451463B1 (en) * | 1997-10-06 | 2002-09-17 | Reveo, Inc. | Electro-chemical power generation systems employing arrays of electronically-controllable discharging and/or recharging cells within a unity support structure |
CN1883072A (en) * | 2003-11-19 | 2006-12-20 | 日产自动车株式会社 | Fuel cell system |
CN1670647A (en) * | 2004-03-19 | 2005-09-21 | 上海神力科技有限公司 | Fuel Cell Controller Regional Bus Distributed Control System |
CN1680822A (en) * | 2004-04-07 | 2005-10-12 | 上海神力科技有限公司 | Voltage detecting monitor of large-scale integrated fuel battery |
CN101351918A (en) * | 2005-12-27 | 2009-01-21 | 日产自动车株式会社 | Fuel cell system |
JP2008177005A (en) * | 2007-01-18 | 2008-07-31 | Matsushita Electric Ind Co Ltd | Fuel cell system |
JP2009283138A (en) * | 2008-05-19 | 2009-12-03 | Honda Motor Co Ltd | Fuel cell system and its operation method |
CN102165637A (en) * | 2008-09-25 | 2011-08-24 | 丰田自动车株式会社 | Fuel cell system and method of detecting abnormality of fuel cell system |
CN102484265A (en) * | 2009-08-21 | 2012-05-30 | 丰田自动车株式会社 | Fuel cell system |
CN102646842A (en) * | 2011-02-22 | 2012-08-22 | 上海攀业氢能源科技有限公司 | Method for improving hydrogen utilization of fuel cell |
CN103293356A (en) * | 2012-02-29 | 2013-09-11 | 欧姆龙株式会社 | Voltage monitoring apparatus and method |
CN104282925A (en) * | 2013-07-11 | 2015-01-14 | 铃木株式会社 | Deterioration detection apparatus for vehicle-used fuel cell |
CN105446288A (en) * | 2015-04-16 | 2016-03-30 | 武汉众宇动力系统科技有限公司 | Fuel cell distributed control system and control method |
CN106374121A (en) * | 2015-07-21 | 2017-02-01 | 通用汽车环球科技运作有限责任公司 | Electrochemical hydrogen sensor for global/local hydrogen starvation detection in PEM fuel cells |
CN109301290A (en) * | 2018-11-23 | 2019-02-01 | 武汉理工大学 | A fuel cell voltage inspection system with flood diagnosis |
EP3866320A1 (en) * | 2020-02-12 | 2021-08-18 | ABB Schweiz AG | Fuel cell power system |
CN113193216A (en) * | 2021-04-25 | 2021-07-30 | 湖北工业大学 | Multi-stack fuel cell system independent of single-chip voltage inspection and control method |
CN113363539A (en) * | 2021-05-28 | 2021-09-07 | 电子科技大学 | High-resolution partition detection system for internal current of fuel cell stack |
CN113793952A (en) * | 2021-08-12 | 2021-12-14 | 上海电气集团股份有限公司 | Fuel cell system and low-temperature starting control method and device thereof |
Non-Patent Citations (2)
Title |
---|
A Novel Method for In-Situ Monitoring of Local Voltage, Temperature and Humidity Distributions in Fuel Cells Using Flexible Multi-Functional Micro Sensors;Chi-Yuan Lee et al.;《Sensors》;第11卷(第2期);第1418页 * |
空冷PEM燃料电池电堆输出功率与水热特性研究;曹颂阳;《中国优秀硕士学位论文全文数据库 工程科技Ⅰ辑》(第第2期期);B015-326 * |
Also Published As
Publication number | Publication date |
---|---|
CN114914492A (en) | 2022-08-16 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN110190306B (en) | Online fault diagnosis method for fuel cell system | |
CN118231883B (en) | Battery management method and system for liquid cooling energy storage system | |
US20050287402A1 (en) | AC impedance monitoring of fuel cell stack | |
CN111693931A (en) | Intelligent electric energy meter error remote calculation method and device and computer equipment | |
US11695138B2 (en) | Device and method for online impedance spectrum measurement of vehicle-mounted hydrogen fuel cell | |
CA2845694C (en) | Power generation characteristic estimation device for fuel cell | |
CN114914492B (en) | Local voltage detection device of fuel cell system and detection analysis method thereof | |
CN119105293B (en) | A method and system for adaptive control of intelligent switch equipment | |
Rubio et al. | Failure mode diagnosis in proton exchange membrane fuel cells using local electrochemical noise | |
CN113629279A (en) | Method and system for controlling working condition of scaling system of multi-source fuel cell | |
CN118100374B (en) | Battery equalization control system based on PID algorithm | |
CN118412499A (en) | Method for judging dryness and humidity degree of hydrogen fuel cell stack and adjusting device thereof | |
CN114156901A (en) | A kind of abnormal state detection method of low voltage distribution transformer reactive power compensation device | |
CN117422254B (en) | Information processing method, device, equipment and storage medium for intelligent park | |
CN117712428A (en) | Rapid diagnosis and self-recovery control method and device for multi-stack fuel cell operation faults | |
CN114415040B (en) | Energy storage power station energy management method and device based on SOC real-time estimation | |
KR102216853B1 (en) | Fuel cell system that sets the way the plant operates | |
KR102219866B1 (en) | fuel cell system that performs self-diagnosis based on the output voltage | |
CN118534222B (en) | Power regulator operation efficiency evaluation system based on data analysis | |
CN109860669B (en) | Fuel Cell Multi-Aspect Online Diagnosis Platform | |
CN113707915B (en) | Water management control method and device for fuel cell stack | |
Jiang et al. | Research on Boiler Energy Saving Technology Based on Internet of Things Data | |
CN118829174B (en) | Self-adaptive heat dissipation control method for electric energy meter | |
CN117332236B (en) | A data tracking and detection method, device and storage medium for a virtual power plant | |
CN119275316B (en) | Optimized control method for hydrogen fuel cell |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant |