CN118522919A - Fuel cell system based on injection humidification - Google Patents
Fuel cell system based on injection humidification Download PDFInfo
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- 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
- H01M8/04082—Arrangements for control of reactant parameters, e.g. pressure or concentration
- H01M8/04089—Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants
- H01M8/04119—Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants with simultaneous supply or evacuation of electrolyte; Humidifying or dehumidifying
- H01M8/04126—Humidifying
- H01M8/04141—Humidifying by water containing exhaust gases
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- 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
- H01M8/04082—Arrangements for control of reactant parameters, e.g. pressure or concentration
- H01M8/04201—Reactant storage and supply, e.g. means for feeding, pipes
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- 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
- H01M8/04694—Processes for controlling fuel cells or fuel cell systems characterised by variables to be controlled
- H01M8/04828—Humidity; Water content
- H01M8/04835—Humidity; Water content of fuel cell reactants
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- 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
- H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
- H01M8/2465—Details of groupings of fuel cells
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- 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
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Abstract
本发明公开了一种基于引射加湿的燃料电池系统,包括电堆、氢气进料管路、第一引射器、第一湿度检测装置、加湿管路、控制阀及控制器,所述氢气进料管路的出口端与电堆连接,所述第一引射器设置于氢气进料管路上,所述第一湿度检测装置也设置于氢气进料管路上且位于第一引射器和电堆之间,所述加湿管路的出口端与第一引射器连接,所述控制阀设置于加湿管路上,所述控制器中预存有理想湿度值,且控制器分别与控制阀和第一湿度检测装置电连接。本发明能够控制燃料电池系统中氢气进料湿度,同时去除了湿空气的水分,使其可以安全进入涡轮发电机,提升了电池性能和系统的可靠性。
The present invention discloses a fuel cell system based on ejection humidification, including a fuel cell stack, a hydrogen feed pipeline, a first ejector, a first humidity detection device, a humidification pipeline, a control valve and a controller, wherein the outlet end of the hydrogen feed pipeline is connected to the fuel cell stack, the first ejector is arranged on the hydrogen feed pipeline, the first humidity detection device is also arranged on the hydrogen feed pipeline and is located between the first ejector and the fuel cell stack, the outlet end of the humidification pipeline is connected to the first ejector, the control valve is arranged on the humidification pipeline, an ideal humidity value is pre-stored in the controller, and the controller is electrically connected to the control valve and the first humidity detection device respectively. The present invention can control the humidity of hydrogen feed in the fuel cell system, and at the same time remove the moisture of the humid air so that it can safely enter the turbine generator, thereby improving the battery performance and the reliability of the system.
Description
技术领域Technical Field
本发明涉及燃料电池技术领域,具体涉及一种基于引射加湿的燃料电池系统。The invention relates to the technical field of fuel cells, and in particular to a fuel cell system based on induced humidification.
背景技术Background Art
在燃料电池中,氢气需要通过进气管道进入电池的膜电极并发生电化学反应,而氢气进料中的湿度对于电池的工作状态和寿命有着重要的影响:氢气进料湿度过高,会使电池产生水滴,在电堆内部造成“水淹”现象,使电池性能下降;氢气进料湿度过低,则会导致质子交换膜的的含水量过低,降低电池性能。目前为氢气进料增加湿度的主流做法是直接将过量的湿氢气通过引射器引射到新氢气当中以增加湿度,然而这种做法无法控制氢气进料的具体湿度,不便于将氢气进料湿度控制在一个比较适宜的范围内,无法充分发挥燃料电池电堆性能。In a fuel cell, hydrogen needs to enter the membrane electrode of the cell through the intake pipe and undergo an electrochemical reaction. The humidity in the hydrogen feed has an important impact on the working state and life of the cell: if the humidity of the hydrogen feed is too high, water droplets will be generated in the cell, causing "flooding" inside the stack and reducing the battery performance; if the humidity of the hydrogen feed is too low, the water content of the proton exchange membrane will be too low, reducing the battery performance. The current mainstream approach to increasing the humidity of the hydrogen feed is to directly inject excess wet hydrogen into the new hydrogen through an injector to increase the humidity. However, this approach cannot control the specific humidity of the hydrogen feed, and is not convenient for controlling the humidity of the hydrogen feed within a more suitable range, and cannot fully exert the performance of the fuel cell stack.
发明内容Summary of the invention
本发明的目的在于克服上述技术不足,提出一种基于引射加湿的燃料电池系统,以解决现有技术中无法控制氢气进料的具体湿度而影响燃料电池电堆性能的技术问题。The purpose of the present invention is to overcome the above technical deficiencies and propose a fuel cell system based on induced humidification to solve the technical problem in the prior art that the specific humidity of the hydrogen feed cannot be controlled, thus affecting the performance of the fuel cell stack.
为达到上述技术目的,本发明采取以下技术方案:In order to achieve the above technical objectives, the present invention adopts the following technical solutions:
本发明提供一种基于引射加湿的燃料电池系统,包括:The present invention provides a fuel cell system based on induced humidification, comprising:
电堆;Battery stack;
氢气进料管路,其出口端与所述电堆连接;A hydrogen feed pipeline, the outlet end of which is connected to the fuel cell stack;
第一引射器,其设置于所述氢气进料管路上;A first ejector, which is arranged on the hydrogen feed pipeline;
第一湿度检测装置,其设置于所述氢气进料管路上且位于所述第一引射器和电堆之间;A first humidity detection device, which is arranged on the hydrogen feed pipeline and located between the first ejector and the fuel cell stack;
加湿管路,其出口端与所述第一引射器连接;A humidification pipeline, the outlet end of which is connected to the first ejector;
控制阀,其设置于所述加湿管路上;A control valve, which is arranged on the humidification pipeline;
控制器,所述控制器中预存有理想湿度值,且所述控制器分别与所述控制阀和第一湿度检测装置电连接。A controller is provided, wherein an ideal humidity value is pre-stored in the controller, and the controller is electrically connected to the control valve and the first humidity detection device respectively.
在一些实施例中,所述燃料电池系统还包括空气进料管路,所述空气进料管路的出口端与所述电堆连接。In some embodiments, the fuel cell system further includes an air feed line, an outlet end of the air feed line is connected to the fuel cell stack.
在一些实施例中,所述燃料电池系统还包括换热器,所述换热器设置于所述空气进料管路上,所述换热器形成有水蒸气出口端和空气出口端,所述水蒸气出口端与所述加湿管路连接,所述空气出口端与所述电堆连接。In some embodiments, the fuel cell system also includes a heat exchanger, which is arranged on the air feed pipeline. The heat exchanger has a water vapor outlet end and an air outlet end. The water vapor outlet end is connected to the humidification pipeline, and the air outlet end is connected to the fuel cell stack.
在一些实施例中,所述燃料电池系统还包括空气压缩机,所述空气压缩机设置于所述换热器来料之前的所述空气进料管路上。In some embodiments, the fuel cell system further includes an air compressor, which is disposed on the air feed pipeline before the heat exchanger.
在一些实施例中,所述燃料电池系统还包括第二湿度检测装置,所述第二湿度检测装置设置于所述空气进料管路上且位于所述换热器和电堆之间。In some embodiments, the fuel cell system further includes a second humidity detection device, which is disposed on the air feed pipeline and located between the heat exchanger and the fuel cell stack.
在一些实施例中,所述燃料电池系统还包括第二引射器,所述第二引射器设置于所述第一引射器来料之前的所述氢气进料管路上。In some embodiments, the fuel cell system further includes a second ejector, which is disposed on the hydrogen feed pipeline before the first ejector.
在一些实施例中,所述燃料电池系统还包括气水分离器和涡轮发电机,所述气水分离器形成有第一入口、第二入口、第一出口以及第二出口,所述第一入口和第二入口分别与所述电堆的过量氢气出口和过量空气出口连接,所述第一出口和第二出口分别与所述第二引射器和涡轮发电机连接。In some embodiments, the fuel cell system also includes a gas-water separator and a turbine generator, the gas-water separator is formed with a first inlet, a second inlet, a first outlet and a second outlet, the first inlet and the second inlet are respectively connected to the excess hydrogen outlet and the excess air outlet of the fuel cell stack, and the first outlet and the second outlet are respectively connected to the second ejector and the turbine generator.
在一些实施例中,所述气水分离器还形成有排水口,所述排水口与所述换热器连接。In some embodiments, the gas-water separator is further formed with a drain port, and the drain port is connected to the heat exchanger.
在一些实施例中,所述气水分离器包括壳体和隔板,所述隔板设置于所述壳体内部将所述壳体内部的空间分隔为第一分离腔和第二分离腔,所述第一分离腔远离所述第二分离腔的一侧开设有所述第一入口,所述第一分离腔顶部开设有所述第一出口,所述第二分离腔远离所述第一分离腔的一侧开设有第二入口,所述第二分离腔顶部开设有所述第二出口,所述排水口开设于所述壳体底部且与所述第一分离腔和第二分离腔均连通。In some embodiments, the gas-water separator includes a shell and a partition, the partition is arranged inside the shell to divide the space inside the shell into a first separation chamber and a second separation chamber, the first separation chamber is provided with the first inlet on the side away from the second separation chamber, the first separation chamber is provided with the first outlet at the top, the second separation chamber is provided with a second inlet on the side away from the first separation chamber, the second separation chamber is provided with the second outlet at the top, and the drain outlet is provided at the bottom of the shell and is connected to both the first separation chamber and the second separation chamber.
在一些实施例中,所述燃料电池系统还包括水蒸气排放管路和空气排放管路,所述水蒸气排放管路与所述控制阀连接,所述空气排放管路与所述涡轮发电机连接。In some embodiments, the fuel cell system further includes a water vapor exhaust pipeline and an air exhaust pipeline, the water vapor exhaust pipeline is connected to the control valve, and the air exhaust pipeline is connected to the turbine generator.
与现有技术相比,本发明提供的一种基于引射加湿的燃料电池系统,通过在第一引射器上连接一个加湿管路,且在所述加湿管路上设置控制阀,则当第一湿度检测装置获取到的氢气进料湿度大于控制器中预存的理想湿度值时,控制控制阀减小开度,使通过第一引射器引射的水蒸气流量减小,从而降低氢气进料管路中的氢气湿度;当第一湿度检测装置获取到的氢气进料湿度小于控制器中预存的理想湿度值时,控制控制阀增大开度,使通过第一引射器引射的水蒸气流量增加,从而提高氢气进料管路中的氢气湿度,如此反复调整可将氢气进料湿度维持在一个合适的数值范围内,以充分利用氢气的能量并避免对电池的损害,提高燃料电池的性能。Compared with the prior art, the present invention provides a fuel cell system based on ejection humidification, which connects a humidification pipeline to the first ejector and sets a control valve on the humidification pipeline. When the hydrogen feed humidity obtained by the first humidity detection device is greater than the ideal humidity value pre-stored in the controller, the control valve is controlled to reduce the opening, so that the water vapor flow ejected through the first ejector is reduced, thereby reducing the hydrogen humidity in the hydrogen feed pipeline; when the hydrogen feed humidity obtained by the first humidity detection device is less than the ideal humidity value pre-stored in the controller, the control valve is controlled to increase the opening, so that the water vapor flow ejected through the first ejector is increased, thereby increasing the hydrogen humidity in the hydrogen feed pipeline. Such repeated adjustments can maintain the hydrogen feed humidity within a suitable numerical range, so as to fully utilize the energy of hydrogen and avoid damage to the battery, thereby improving the performance of the fuel cell.
附图说明BRIEF DESCRIPTION OF THE DRAWINGS
图1是本发明实施例提供的基于引射加湿的燃料电池系统的结构框图;FIG1 is a structural block diagram of a fuel cell system based on induced humidification provided by an embodiment of the present invention;
图2是本发明实施例提供的所述气水分离器的结构示意图;FIG2 is a schematic structural diagram of the gas-water separator provided in an embodiment of the present invention;
图3是本发明实施例提供的基于引射加湿的燃料电池系统的工作原理图。FIG3 is a working principle diagram of a fuel cell system based on induced humidification according to an embodiment of the present invention.
附图标记说明如下:The following are the descriptions of the reference numerals:
1、电堆,2、氢气进料管路,3、第一引射器,4、第一湿度检测装置,5、加湿管路,6、控制阀,7、空气进料管路,8、换热器,9、空气压缩机,10、第二湿度检测装置,11、第二引射器,12、气水分离器,121、第一入口,122、第一出口,123、第二入口,124、第二出口,125、排水口,126、壳体,127、隔板,13、涡轮发电机,14、水蒸气排放管路,15、空气排放管路。1. Fuel cell, 2. Hydrogen feed pipeline, 3. First ejector, 4. First humidity detection device, 5. Humidification pipeline, 6. Control valve, 7. Air feed pipeline, 8. Heat exchanger, 9. Air compressor, 10. Second humidity detection device, 11. Second ejector, 12. Gas-water separator, 121. First inlet, 122. First outlet, 123. Second inlet, 124. Second outlet, 125. Drain, 126. Shell, 127. Partition, 13. Turbine generator, 14. Water vapor exhaust pipeline, 15. Air exhaust pipeline.
具体实施方式DETAILED DESCRIPTION
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仅用以解释本发明,并不用于限定本发明。In order to make the purpose, technical solution and advantages of the present invention more clearly understood, the present invention is further described in detail below in conjunction with the accompanying drawings and embodiments. It should be understood that the specific embodiments described herein are only used to explain the present invention and are not intended to limit the present invention.
为了实现控制燃料电池系统中氢气进料的具体湿度的技术问题,本发明提供一种基于引射加湿的燃料电池系统,能够控制燃料电池系统中氢气进堆的具体湿度,以提高电池电堆性能。In order to solve the technical problem of controlling the specific humidity of hydrogen feed in a fuel cell system, the present invention provides a fuel cell system based on induced humidification, which can control the specific humidity of hydrogen feed in the fuel cell system to improve the performance of the battery stack.
请参阅图1,图1为本发明一实施例的一种基于引射加湿的燃料电池系统的结构框图,所述燃料电池系统包括电堆1、氢气进料管路2、第一引射器3、第一湿度检测装置4、加湿管路5、控制阀6以及控制器,所述电堆1为燃料电池系统的核心部件,用于氢气与氧气发生反应以产生电能,所述氢气进料管路2的入口端与外部氢气源连接,所述氢气进料管路2的出口端与所述电堆1连接,用于为电堆1的反应提供氢气;所述第一引射器3设置于氢气进料管路2上,所述第一湿度检测装置4也设置于氢气进料管路2上,用于实时获取氢气进料管路2中的氢气进料湿度;所述加湿管路5的入口端与水蒸气供给设备连接,所述加湿管路5的出口端与第一引射器3连接,将加湿管路5中的水蒸气输送至第一引射器3中,用于增加第一引射器3中的氢气湿度;所述控制阀6设置于所述加湿管路5上,用于控制加湿管路5中的水蒸气的排放量;所述控制器中预存有理想湿度值,且所述控制器分别与所述控制阀6和第一湿度检测装置4电连接。Please refer to Figure 1, which is a structural block diagram of a fuel cell system based on ejection humidification according to an embodiment of the present invention. The fuel cell system includes a fuel cell stack 1, a hydrogen feed pipeline 2, a first ejector 3, a first humidity detection device 4, a humidification pipeline 5, a control valve 6 and a controller. The fuel cell stack 1 is a core component of the fuel cell system, which is used for hydrogen and oxygen to react to generate electrical energy. The inlet end of the hydrogen feed pipeline 2 is connected to an external hydrogen source, and the outlet end of the hydrogen feed pipeline 2 is connected to the fuel cell stack 1 to provide hydrogen for the reaction of the fuel cell stack 1; the first ejector 3 is arranged on the hydrogen feed pipeline 2, The first humidity detection device 4 is also arranged on the hydrogen feed pipeline 2, and is used to obtain the hydrogen feed humidity in the hydrogen feed pipeline 2 in real time; the inlet end of the humidification pipeline 5 is connected to the water vapor supply equipment, and the outlet end of the humidification pipeline 5 is connected to the first ejector 3, and the water vapor in the humidification pipeline 5 is transported to the first ejector 3, so as to increase the humidity of the hydrogen in the first ejector 3; the control valve 6 is arranged on the humidification pipeline 5, and is used to control the discharge amount of the water vapor in the humidification pipeline 5; the ideal humidity value is pre-stored in the controller, and the controller is electrically connected to the control valve 6 and the first humidity detection device 4 respectively.
本实施例中,在氢气进料管路2上设置第一引射器3,且第一引射器3与加湿管路5连接,可将加湿管路5中的水蒸气传送至第一引射器3中,与氢气混合后引射至电堆1中进行反应,在此过程中,为了控制氢气进料湿度,我们在第一引射器3与电堆1之间的氢气进料管路2上设置了第一湿度检测装置4,并且在加湿管路5上设置了控制阀6,则当第一湿度检测装置4获取到的实际氢气进料湿度大于控制器中预存的理想湿度值时,控制器就会控制控制阀6减小开度,使通过第一引射器3引射的水蒸气流量减小,从而降低氢气进料管路2中的氢气湿度;而当第一湿度检测装置4获取到的实际氢气进料湿度小于控制器中预存的理想湿度值时,控制器就会控制控制阀6增大开度,使通过第一引射器3引射的水蒸气流量增加,从而提高氢气进料管路2中的氢气湿度,如此反复调整可将氢气进料湿度维持在一个合适的数值范围内,以充分利用氢气的能量并避免对电池的损害,达到提高燃料电池性能的目的。In this embodiment, a first ejector 3 is provided on the hydrogen feed pipeline 2, and the first ejector 3 is connected to the humidification pipeline 5, so that the water vapor in the humidification pipeline 5 can be transferred to the first ejector 3, mixed with hydrogen and then ejected into the fuel cell stack 1 for reaction. In this process, in order to control the humidity of the hydrogen feed, a first humidity detection device 4 is provided on the hydrogen feed pipeline 2 between the first ejector 3 and the fuel cell stack 1, and a control valve 6 is provided on the humidification pipeline 5. When the actual hydrogen feed humidity obtained by the first humidity detection device 4 is greater than the ideal humidity value pre-stored in the controller, the controller will control the control valve 6. The valve 6 reduces its opening degree, thereby reducing the flow rate of water vapor ejected through the first ejector 3, thereby reducing the humidity of hydrogen in the hydrogen feed pipeline 2; and when the actual hydrogen feed humidity obtained by the first humidity detection device 4 is less than the ideal humidity value pre-stored in the controller, the controller will control the control valve 6 to increase its opening degree, thereby increasing the flow rate of water vapor ejected through the first ejector 3, thereby increasing the humidity of hydrogen in the hydrogen feed pipeline 2. Such repeated adjustments can maintain the hydrogen feed humidity within a suitable numerical range, so as to fully utilize the energy of hydrogen and avoid damage to the battery, thereby achieving the purpose of improving the performance of the fuel cell.
在其中一个实施例中,所述燃料电池系统还包括空气进料管路7,所述空气进料管路7的入口端与外部空气源连接,所述空气进料管路7的出口端与所述电堆1连接,为电堆1反应提供空气。In one of the embodiments, the fuel cell system further includes an air feed line 7, the inlet end of the air feed line 7 is connected to an external air source, and the outlet end of the air feed line 7 is connected to the fuel cell stack 1 to provide air for the fuel cell stack 1 reaction.
本实施例中,空气进料管路7的另一个作用是为加湿管路5提供水蒸气,而水蒸气的产生一般需要使用换热器8,因此,在其中一个实施例中,所述燃料电池系统还包括换热器8,所述换热器8设置于所述空气进料管路7上,所述换热器8形成有水蒸气出口端和空气出口端,所述水蒸气出口端与所述加湿管路5连接,所述空气出口端与所述电堆1连接。In this embodiment, another function of the air feed pipeline 7 is to provide water vapor for the humidification pipeline 5, and the generation of water vapor generally requires the use of a heat exchanger 8. Therefore, in one of the embodiments, the fuel cell system also includes a heat exchanger 8, and the heat exchanger 8 is arranged on the air feed pipeline 7. The heat exchanger 8 is formed with a water vapor outlet end and an air outlet end, and the water vapor outlet end is connected to the humidification pipeline 5, and the air outlet end is connected to the fuel cell stack 1.
在其中一个实施例中,所述燃料电池系统还包括空气压缩机9,所述空气压缩机9设置于所述换热器8来料之前的所述空气进料管路7上。In one embodiment, the fuel cell system further includes an air compressor 9 , which is disposed on the air feed pipeline 7 before the heat exchanger 8 .
本实施例中,空气在空气压缩机9的压缩作用下变为高温高压的气体进入至空气进料管路7中,进而进入至换热器8中,换热器8中的液态水被高温空气加热后形成水蒸气以待进入加湿管路5中,同时,降温后的空气进入至电堆1中参与反应。In this embodiment, the air is compressed by the air compressor 9 and becomes a high-temperature and high-pressure gas, which enters the air feed pipeline 7 and then enters the heat exchanger 8. The liquid water in the heat exchanger 8 is heated by the high-temperature air to form water vapor to be entered into the humidification pipeline 5. At the same time, the cooled air enters the fuel cell stack 1 to participate in the reaction.
在其中一个实施例中,所述燃料电池系统还包括第二湿度检测装置10,所述第二湿度检测装置10设置于所述空气进料管路7上且位于所述换热器8和电堆1之间,用于检测空气进料的湿度。In one of the embodiments, the fuel cell system further includes a second humidity detection device 10, which is disposed on the air feed pipeline 7 and located between the heat exchanger 8 and the fuel cell stack 1, and is used to detect the humidity of the air feed.
在其中一个实施例中,所述燃料电池系统还包括第二引射器11,所述第二引射器11设置于所述第一引射器3来料之前的所述氢气进料管路2上,用于氢气源与电堆1反应后的过量氢气的混合引射。In one embodiment, the fuel cell system further includes a second ejector 11, which is disposed on the hydrogen feed pipeline 2 before the first ejector 3, and is used for mixing and ejecting excess hydrogen after the hydrogen source reacts with the fuel cell stack 1.
在其中一个实施例中,所述燃料电池系统还包括气水分离器12和涡轮发电机13,所述气水分离器12形成有第一入口121、第一出口122、第二入口123以及第二出口124,所述第一入口121和第二入口123分别与所述电堆1的过量氢气出口和过量空气出口连接,所述第一出口122和第二出口124分别与所述第二引射器11和涡轮发电机13连接。In one embodiment, the fuel cell system also includes a gas-water separator 12 and a turbine generator 13, the gas-water separator 12 is formed with a first inlet 121, a first outlet 122, a second inlet 123 and a second outlet 124, the first inlet 121 and the second inlet 123 are respectively connected to the excess hydrogen outlet and the excess air outlet of the fuel cell stack 1, and the first outlet 122 and the second outlet 124 are respectively connected to the second ejector 11 and the turbine generator 13.
也就是说,本实施例中,电堆1反应后的剩余氢气经过气水分离器12的分离作用回流至第二引射器11继续参与反应,而剩余空气经过气水分离器12的分离作用被送至涡轮发电机13进行发电,以回收利用能量,此处设置的气水分离器12能够充分分离过剩空气中的水分,与现有技术相比,除去水分的空气被送往涡轮发电机13进行发电,不会损坏涡轮发电机13的叶轮,对设备的保护具有重要意义。That is to say, in this embodiment, the remaining hydrogen after the reaction of the fuel cell stack 1 is returned to the second ejector 11 through the separation effect of the gas-water separator 12 to continue to participate in the reaction, while the remaining air is sent to the turbine generator 13 for power generation through the separation effect of the gas-water separator 12 to recycle energy. The gas-water separator 12 arranged here can fully separate the moisture in the excess air. Compared with the prior art, the air with moisture removed is sent to the turbine generator 13 for power generation, which will not damage the impeller of the turbine generator 13, and is of great significance to the protection of the equipment.
在其中一个实施例中,所述气水分离器12还形成有排水口125,所述排水口125与所述换热器8连接,将气水分离的液态水传送至换热器8中,为换热器8供给加湿管路5水蒸气提供水源,节约了能源。In one embodiment, the gas-water separator 12 is further formed with a drain port 125, and the drain port 125 is connected to the heat exchanger 8 to transfer the liquid water separated from the gas and water to the heat exchanger 8, providing a water source for the heat exchanger 8 to supply water vapor to the humidification pipeline 5, thereby saving energy.
在其中一个实施例中,所述燃料电池系统还包括水蒸气排放管路14和空气排放管路15,所述水蒸气排放管路14与所述控制阀6连接,所述空气排放管路15与所述涡轮发电机13连接,水蒸气排放管路14用于将加湿管路5中多余的水蒸气排放至系统外部,空气排放管路15用于将通过涡轮发电机13发电的空气排放至系统以外的大气中。In one embodiment, the fuel cell system further includes a water vapor exhaust pipeline 14 and an air exhaust pipeline 15, wherein the water vapor exhaust pipeline 14 is connected to the control valve 6, and the air exhaust pipeline 15 is connected to the turbine generator 13, the water vapor exhaust pipeline 14 is used to discharge excess water vapor in the humidification pipeline 5 to the outside of the system, and the air exhaust pipeline 15 is used to discharge air generated by power generation by the turbine generator 13 to the atmosphere outside the system.
在其中一个实施例中,请参阅图2所示,所述气水分离器12为二进二出式气水分离器,其包括壳体126和隔板127,所述隔板127设置于所述壳体126内部将所述壳体126内部的空间分隔为第一分离腔和第二分离腔,第一分离腔和第二分离腔在本实施例中分别用于分离氢气水蒸气和空气水蒸气,在本实施例以外的实施例中,还可用于分离另外两种不同的气水混合物。In one of the embodiments, please refer to FIG. 2 , the gas-water separator 12 is a two-in-two-out type gas-water separator, which includes a shell 126 and a partition 127. The partition 127 is arranged inside the shell 126 to separate the space inside the shell 126 into a first separation chamber and a second separation chamber. The first separation chamber and the second separation chamber are used to separate hydrogen water vapor and air water vapor, respectively, in this embodiment. In embodiments other than this embodiment, they can also be used to separate two other different gas-water mixtures.
本实施例中,所述第一分离腔远离所述第二分离腔的一侧开设有所述第一入口121,所述第一分离腔顶部开设有所述第一出口122,第一入口121用于进入过量的氢气和水的混合物,第一出口122用于输出分离后的氢气,因此,第一入口121与电堆1的过量氢气出口连接,第一出口122与第二引射器11连接;所述第二分离腔远离所述第一分离腔的一侧开设有第二入口123,所述第二分离腔顶部开设有所述第二出口124,第二入口123用于进入过量的空气和水的混合物,第二出口124用于为涡轮发电机13输入干燥空气,因此,第二入口123与电堆1的过量空气出口连接,第二出口124与涡轮发电机13连接。In this embodiment, the first inlet 121 is provided on the side of the first separation chamber away from the second separation chamber, and the first outlet 122 is provided on the top of the first separation chamber. The first inlet 121 is used to enter a mixture of excess hydrogen and water, and the first outlet 122 is used to output the separated hydrogen. Therefore, the first inlet 121 is connected to the excess hydrogen outlet of the fuel cell stack 1, and the first outlet 122 is connected to the second ejector 11; the second inlet 123 is provided on the side of the second separation chamber away from the first separation chamber, and the second outlet 124 is provided on the top of the second separation chamber. The second inlet 123 is used to enter a mixture of excess air and water, and the second outlet 124 is used to input dry air to the turbine generator 13. Therefore, the second inlet 123 is connected to the excess air outlet of the fuel cell stack 1, and the second outlet 124 is connected to the turbine generator 13.
在其中一个实施例中,请参阅图2所示,所述排水口125开设于所述壳体126底部且与所述第一分离腔和第二分离腔均连通,第一分离腔和第二分离腔分离后的液态水通过排水口125排出气水分离器12,而排水口125与换热器8连接,因此,气水分离器12排出的液态水进入至换热器8中为水蒸气的形成提供水源,有效利用了资源。In one of the embodiments, please refer to Figure 2, the drain port 125 is opened at the bottom of the shell 126 and is connected to the first separation chamber and the second separation chamber. The liquid water separated from the first separation chamber and the second separation chamber is discharged from the gas-water separator 12 through the drain port 125, and the drain port 125 is connected to the heat exchanger 8. Therefore, the liquid water discharged from the gas-water separator 12 enters the heat exchanger 8 to provide a water source for the formation of water vapor, thereby effectively utilizing resources.
为了更好的理解本发明,以下结合图3对本发明技术方案的工作原理进行如下说明:In order to better understand the present invention, the working principle of the technical solution of the present invention is described as follows in conjunction with FIG3:
首先,在控制器中预存一个氢气进料的理想湿度,标记为RH0;First, an ideal humidity of hydrogen feed is pre-stored in the controller, marked as RH0;
之后,通过第一湿度检测装置4检测氢气进料管路2中的氢气湿度RH,当RH>RH0时,由控制器控制控制阀6减小其开度,使通过第一引射器3的水蒸气流量减小,从而降低氢气进料的湿度;Afterwards, the first humidity detection device 4 detects the humidity RH of the hydrogen in the hydrogen feed pipeline 2. When RH>RH0, the controller controls the control valve 6 to reduce its opening, so that the water vapor flow through the first ejector 3 is reduced, thereby reducing the humidity of the hydrogen feed;
当RH<RH0时,由控制器控制阀6增大其开度,使通过第一引射器3的水蒸气流量增大,从而提高氢气进料的湿度;When RH<RH0, the controller controls the valve 6 to increase its opening, so that the water vapor flow through the first ejector 3 increases, thereby increasing the humidity of the hydrogen feed;
当RH=RH0时,固定此时控制阀6的开度,使通过第一引射器3的水蒸气流量维持在当时状态,从而保持当前氢气进料的湿度。When RH=RH0, the opening of the control valve 6 is fixed at this time to maintain the water vapor flow through the first ejector 3 at the current state, thereby maintaining the humidity of the current hydrogen feed.
需要说明的是,通常情况下,燃料电池的氢气进料湿度控制在30%~70%的范围内较为适宜,能够充分利用氢气的能量并且避免对电池的损害。同时,在不同工作条件下,还需要根据具体情况进行湿度的调节,并且定期维护氢气进料管路2,防止氢气进料管路2受潮,以确保电池的正常工作。It should be noted that, under normal circumstances, it is more appropriate to control the hydrogen feed humidity of the fuel cell within the range of 30% to 70%, which can fully utilize the energy of hydrogen and avoid damage to the battery. At the same time, under different working conditions, it is necessary to adjust the humidity according to the specific situation, and regularly maintain the hydrogen feed pipeline 2 to prevent the hydrogen feed pipeline 2 from getting wet, so as to ensure the normal operation of the battery.
另外,本发明中所述的控制阀6为三通阀,第一湿度检测装置4和第二湿度检测装置10为温湿度检测仪。In addition, the control valve 6 described in the present invention is a three-way valve, and the first humidity detection device 4 and the second humidity detection device 10 are temperature and humidity detectors.
以上所述本发明的具体实施方式,并不构成对本发明保护范围的限定。任何根据本发明的技术构思所做出的各种其他相应的改变与变形,均应包含在本发明权利要求的保护范围内。The specific implementation of the present invention described above does not constitute a limitation on the protection scope of the present invention. Any other corresponding changes and modifications made based on the technical concept of the present invention should be included in the protection scope of the claims of the present invention.
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