CN115224326A - A kind of fuel cell air control method using molecular sieve - Google Patents

A kind of fuel cell air control method using molecular sieve Download PDF

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CN115224326A
CN115224326A CN202110425827.7A CN202110425827A CN115224326A CN 115224326 A CN115224326 A CN 115224326A CN 202110425827 A CN202110425827 A CN 202110425827A CN 115224326 A CN115224326 A CN 115224326A
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molecular sieve
air
fuel cell
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周百慧
方川
洪坡
赵兴旺
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Beijing Sinohytec Co Ltd
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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/06Combination of fuel cells with means for production of reactants or for treatment of residues
    • H01M8/0662Treatment of gaseous reactants or gaseous residues, e.g. cleaning
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04082Arrangements for control of reactant parameters, e.g. pressure or concentration
    • H01M8/04089Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants
    • H01M8/04097Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants with recycling of the reactants
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04082Arrangements for control of reactant parameters, e.g. pressure or concentration
    • H01M8/04089Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants
    • H01M8/04119Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants with simultaneous supply or evacuation of electrolyte; Humidifying or dehumidifying
    • H01M8/04156Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants with simultaneous supply or evacuation of electrolyte; Humidifying or dehumidifying with product water removal
    • H01M8/04179Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants with simultaneous supply or evacuation of electrolyte; Humidifying or dehumidifying with product water removal by purging or increasing flow or pressure of reactants
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/06Combination of fuel cells with means for production of reactants or for treatment of residues
    • H01M8/0662Treatment of gaseous reactants or gaseous residues, e.g. cleaning
    • H01M8/0687Reactant purification by the use of membranes or filters
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells

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Abstract

本发明涉及燃料电池领域,具体涉及一种利用分子筛的燃料电池空气控制方法,包括在空气进气管路中将分子筛设置在空压机的下游,并将所述分子筛设置在中冷器与燃料电池电堆之间,利用空压机增加分子筛的吸附压力,分子筛吸附空气中的氮气;空压机将分子筛吸附后的空气输入燃料电池电堆的阴极室入口;降低分子筛的吸附压力,将分子筛吸附的氮气脱附,并通过氮气脱附管路排出至大气。本发明通过控制空压机的压力及管路的切换使分子筛吸附通过中冷器的空气,使氮气从空气中分离被吸附到分子筛,提升进入电堆中空气的氧气浓度,提高电堆的性能;将空压机设置在分子筛之前,分子筛的工作效率更高,寿命更长,另外被吸附在分子筛的氮气还能够通过调节压力被脱附,脱附的氮气能够直接用于电堆的吹扫,降低吹扫后的氧气残留,避免残留氧气对电堆造成的损害。

Figure 202110425827

The invention relates to the field of fuel cells, in particular to a fuel cell air control method using molecular sieves, which comprises arranging the molecular sieve downstream of an air compressor in an air intake pipeline, and arranging the molecular sieve between an intercooler and a fuel cell. Between the stacks, the air compressor is used to increase the adsorption pressure of the molecular sieve, and the molecular sieve adsorbs nitrogen in the air; the air compressor feeds the air adsorbed by the molecular sieve into the inlet of the cathode chamber of the fuel cell stack; reduces the adsorption pressure of the molecular sieve and adsorbs the molecular sieve The nitrogen is desorbed and discharged to the atmosphere through the nitrogen desorption pipeline. By controlling the pressure of the air compressor and the switching of the pipeline, the invention makes the molecular sieve adsorb the air passing through the intercooler, so that the nitrogen is separated from the air and adsorbed to the molecular sieve, so that the oxygen concentration of the air entering the stack is increased, and the performance of the stack is improved. ; Set the air compressor before the molecular sieve, the molecular sieve has a higher working efficiency and a longer life, and the nitrogen adsorbed on the molecular sieve can also be desorbed by adjusting the pressure, and the desorbed nitrogen can be directly used for the purging of the stack , reduce the residual oxygen after purging, and avoid the damage caused by residual oxygen to the stack.

Figure 202110425827

Description

一种利用分子筛的燃料电池空气控制方法A kind of fuel cell air control method using molecular sieve

技术领域technical field

本发明涉及燃料电池领域,具体涉及一种利用分子筛的燃料电池空气控制方法。The invention relates to the field of fuel cells, in particular to a fuel cell air control method using molecular sieves.

背景技术Background technique

氧气是燃料电池的重要反应原料,现有燃料电池系统技术仅利用环境空气作为原料,并不对其进行任何成分处理,现有技术的空气系统由空滤、空压机、中冷器、增湿器组成,并配有节气门和三通阀等调节气体压力,氧气的浓度只能由空气流量中的氧气浓度决定,无法调节。由于氧气浓度的提高可以提高电堆性能,而自然环境中的空气氧含量太低,燃料电池入堆氧气浓度无法提高,限制了电堆的发电功率;另外,在吹扫电堆时,现有技术电堆的吹扫模式采用空气吹扫,吹扫后会有空气中的氧气残留,而氧气残留则会对电堆造成损害;上述方法均不利于提高系统效率和可靠性。而现有技术中尚没有能够较好的解决燃料电池系统调节空气中氧浓度的技术方案。Oxygen is an important reaction raw material for fuel cells. The existing fuel cell system technology only uses ambient air as a raw material without any component treatment. The existing air system consists of air filtration, air compressors, intercoolers, humidifiers. It is equipped with a throttle valve and a three-way valve to adjust the gas pressure. The concentration of oxygen can only be determined by the oxygen concentration in the air flow and cannot be adjusted. Since the increase of oxygen concentration can improve the performance of the stack, the oxygen content of the air in the natural environment is too low, the oxygen concentration of the fuel cell into the stack cannot be increased, which limits the power generation of the stack; in addition, when the stack is purged, the existing The purging mode of the technical stack adopts air purging. After purging, there will be residual oxygen in the air, and the residual oxygen will cause damage to the stack. The above methods are not conducive to improving the efficiency and reliability of the system. However, in the prior art, there is still no technical solution that can better solve the problem of adjusting the oxygen concentration in the air by the fuel cell system.

发明内容SUMMARY OF THE INVENTION

鉴于现有技术中存在的技术缺陷和技术弊端,本发明实施例提供克服上述问题或者至少部分地解决上述问题的一种利用分子筛的燃料电池空气控制方法,利用分子筛分离技术解决了燃料电池阴极中氧含量对电堆的限制问题。In view of the technical defects and technical drawbacks existing in the prior art, the embodiments of the present invention provide a fuel cell air control method using molecular sieves that overcomes the above problems or at least partially solves the above problems. The limitation of oxygen content on the stack.

本发明实施例提供了一种利用分子筛的燃料电池空气控制方法,所述燃料电池空气控制方法包括,An embodiment of the present invention provides a fuel cell air control method using molecular sieves, and the fuel cell air control method includes:

在空气进气管路中将分子筛设置在空压机的下游,并将所述分子筛设置在中冷器与燃料电池电堆之间,利用空压机增加分子筛的吸附压力,分子筛吸附空气中的氮气;The molecular sieve is arranged downstream of the air compressor in the air intake pipeline, and the molecular sieve is arranged between the intercooler and the fuel cell stack. The air compressor is used to increase the adsorption pressure of the molecular sieve, and the molecular sieve adsorbs nitrogen in the air. ;

空压机将分子筛吸附后的空气输入燃料电池电堆的阴极室入口;The air compressor feeds the air adsorbed by the molecular sieve into the inlet of the cathode chamber of the fuel cell stack;

降低分子筛的吸附压力,将分子筛吸附的氮气脱附,并通过氮气脱附管路排出至大气。Reduce the adsorption pressure of the molecular sieve, desorb the nitrogen adsorbed by the molecular sieve, and discharge it to the atmosphere through the nitrogen desorption pipeline.

进一步地,所述燃料电池空气控制方法包括,Further, the fuel cell air control method includes:

至少设置第一分子筛与第二分子筛,将第一分子筛、第二分子筛分别与空压机、氮气脱附管路连接;At least a first molecular sieve and a second molecular sieve are arranged, and the first molecular sieve and the second molecular sieve are respectively connected to the air compressor and the nitrogen desorption pipeline;

当第一分子筛与空压机连通时,控制第二分子筛与氮气脱附管路连通;当第二分子筛与空压机连通时,控制第一分子筛与氮气脱附管路连通。When the first molecular sieve is communicated with the air compressor, the second molecular sieve is controlled to communicate with the nitrogen desorption pipeline; when the second molecular sieve is communicated with the air compressor, the first molecular sieve is controlled to communicate with the nitrogen desorption pipeline.

进一步地,所述燃料电池空气控制方法包括,Further, the fuel cell air control method includes:

设置空气补充路,所述空气补充路的进气口设置在空压机与中冷器之间的空气进气管路,所述空气补充路的出气口设置在分子筛与燃料电池电堆之间的空气进气管路,通过空气补充路调节进入燃料电池电堆的氧气浓度。An air supplementary circuit is provided, the air inlet of the air supplementary circuit is arranged in the air intake pipeline between the air compressor and the intercooler, and the air outlet of the air supplementary circuit is arranged in the air inlet between the molecular sieve and the fuel cell stack. The air intake line adjusts the oxygen concentration entering the fuel cell stack through the air supplementary line.

进一步地,所述燃料电池空气控制方法包括,Further, the fuel cell air control method includes:

根据燃料电池电堆性能确定入堆的氧气浓度目标需求;Determine the target requirement of oxygen concentration into the stack according to the performance of the fuel cell stack;

通过控制空气补充路阀门的开度分配空气进气管路与空气补充路的空气流量。By controlling the opening of the air supplementary circuit valve, the air flow of the air intake line and the air supplementary circuit is distributed.

进一步地,所述燃料电池空气控制方法包括,按照预设条件控制第一分子筛及第二分子筛与空压机交替连通。Further, the fuel cell air control method includes controlling the first molecular sieve and the second molecular sieve to communicate alternately with the air compressor according to preset conditions.

进一步地,所述燃料电池空气控制方法包括,Further, the fuel cell air control method includes:

所述预设条件为根据燃料电池工况及分子筛的性能确定的交替设定时间,当达到交替设定时间时,切换第一分子筛、第二分子筛与空压机之间的阀门。The preset condition is an alternate setting time determined according to the working conditions of the fuel cell and the performance of the molecular sieve. When the alternate setting time is reached, the valves between the first molecular sieve, the second molecular sieve and the air compressor are switched.

进一步地,所述燃料电池空气控制方法包括,Further, the fuel cell air control method includes:

通过断开分子筛与空压机的连通降低分子筛的吸附压力,使分子筛脱附氮气;Reduce the adsorption pressure of the molecular sieve by disconnecting the connection between the molecular sieve and the air compressor, so that the molecular sieve can desorb nitrogen;

在燃料电池工作模式下,将氮气通过氮气脱附管路的氮气排出支路排出至大气;In the working mode of the fuel cell, the nitrogen is discharged to the atmosphere through the nitrogen discharge branch of the nitrogen desorption pipeline;

在燃料电池吹扫模式下,将氮气通过氮气脱附管路的氮气吹扫支路输入燃料电池电堆的阴极室入口。In the fuel cell purge mode, nitrogen is fed into the cathode chamber inlet of the fuel cell stack through the nitrogen purge branch of the nitrogen desorption pipeline.

进一步地,所述燃料电池空气控制方法还包括,Further, the fuel cell air control method further includes:

根据燃料电池系统的关机状态确定吹扫时机;Determine the purging timing according to the shutdown state of the fuel cell system;

当判定到达吹扫时机时,启动燃料电池吹扫模式,关闭氮气排出支路的阀门;When it is determined that the purging opportunity is reached, the fuel cell purging mode is activated, and the valve of the nitrogen discharge branch is closed;

降低空压机转速,减小空压机下游的阀门的开度。Reduce the speed of the air compressor and reduce the opening of the valve downstream of the air compressor.

本发明实施例能够至少部分实现如下技术效果:The embodiments of the present invention can at least partially achieve the following technical effects:

本发明为控制分子筛设置在空压机的下游的燃料电池空气系统的方法,分子筛与空压机之间设置中冷器,通过控制空压机的压力及管路的切换使分子筛吸附通过中冷器的空气,使氮气从空气中分离被吸附到分子筛,提升进入电堆中空气的氧气浓度,从而提高电堆的性能;而且,将空压机设置在分子筛之前,分子筛的工作效率更高,寿命更长,另外被吸附在分子筛的氮气还能够通过调节压力被脱附,脱附的氮气能够直接用于电堆的吹扫,降低吹扫后的氧气残留,避免残留氧气对电堆造成的损害。The present invention is a method for controlling the air system of a fuel cell where the molecular sieve is arranged downstream of the air compressor. An intercooler is arranged between the molecular sieve and the air compressor, and the molecular sieve is adsorbed through the intercooler by controlling the pressure of the air compressor and the switching of the pipeline. air from the air compressor, so that nitrogen is separated from the air and adsorbed to the molecular sieve, which increases the oxygen concentration of the air entering the stack, thereby improving the performance of the stack; moreover, if the air compressor is set before the molecular sieve, the molecular sieve works more efficiently Longer life, in addition, the nitrogen adsorbed on the molecular sieve can be desorbed by adjusting the pressure, and the desorbed nitrogen can be directly used for the purging of the stack, reducing the residual oxygen after purging, and avoiding the residual oxygen to the stack. damage.

本发明的其它特征和优点将在随后的说明书中阐述,并且,部分地从说明书中变得显而易见,或者通过实施本发明而了解。本发明的目的和其他优点可通过在所写的说明书、以及附图中所记载的结构来实现和获得。Other features and advantages of the present invention will be set forth in the description which follows, and in part will be apparent from the description, or may be learned by practice of the invention. The objectives and other advantages of the invention may be realized and attained by the structure described in the written description and appended drawings.

下面通过附图和实施例,对本发明的技术方案做进一步的详细描述。The technical solutions of the present invention will be further described in detail below through the accompanying drawings and embodiments.

附图说明Description of drawings

附图用来提供对本发明的进一步理解,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,并不构成对本发明的限制。在附图中:The accompanying drawings are used to provide a further understanding of the present invention, and constitute a part of the specification, and are used to explain the present invention together with the embodiments of the present invention, and do not constitute a limitation to the present invention. In the attached image:

图1为本发明一实施例的利用分子筛的燃料电池空气处理系统的示意图。FIG. 1 is a schematic diagram of a fuel cell air treatment system utilizing molecular sieves according to an embodiment of the present invention.

图2为本发明一实施例的利用分子筛的燃料电池空气控制方法的流程图。FIG. 2 is a flowchart of a fuel cell air control method using molecular sieves according to an embodiment of the present invention.

图3为本发明一实施例的利用分子筛的低尾排燃料电池空气处理系统的示意图。FIG. 3 is a schematic diagram of a low tail emission fuel cell air treatment system using molecular sieves according to an embodiment of the present invention.

图4为本发明一实施例的利用分子筛的低尾排燃料电池空气控制方法的流程图。FIG. 4 is a flowchart of a method for controlling air in a low tail emission fuel cell using molecular sieves according to an embodiment of the present invention.

图5为本发明一实施例的利用分子筛的氧气循环燃料电池空气处理系统的示意图。5 is a schematic diagram of an oxygen cycle fuel cell air treatment system using molecular sieves according to an embodiment of the present invention.

图6为本发明一实施例的利用分子筛的氧气循环燃料电池空气控制方法的流程图。6 is a flow chart of a method for controlling air in an oxygen-circulating fuel cell using molecular sieves according to an embodiment of the present invention.

附图说明:1、燃料电池电堆;2、空气进气管路;3、氮气脱附管路;4、空气补充路;5、氢气尾排管路;6、氧气循环路;21、空滤;22、空压机;23、分子筛;24、中冷器;25、增湿器;31、氮气排出支路;32、氮气吹扫支路;33、氮气尾排支路。Description of the drawings: 1. Fuel cell stack; 2. Air intake pipeline; 3. Nitrogen desorption pipeline; 4. Air supplementary pipeline; 5. Hydrogen tail exhaust pipeline; 6. Oxygen circulation circuit; 21. Air filter 22, air compressor; 23, molecular sieve; 24, intercooler; 25, humidifier; 31, nitrogen discharge branch; 32, nitrogen purge branch; 33, nitrogen tail discharge branch.

具体实施方式Detailed ways

为详细说明本发明的技术内容、所实现目的及效果,以下结合实施方式并配合附图予以说明。In order to describe in detail the technical content, achieved objects and effects of the present invention, the following descriptions are given with reference to the embodiments and the accompanying drawings.

附图和以下说明描述了本发明的可选实施方式以教导本领域技术人员如何实施和再现本发明。为了教导本发明技术方案,已简化或省略了一些常规方面。本领域技术人员应该理解源自这些实施方式的变型或替换将落在本发明的保护范围内。本领域技术人员应该理解下述特征能够以各种方式组合以形成本发明的多个变型。The drawings and the following description describe alternative embodiments of the invention to teach those skilled in the art how to practice and reproduce the invention. In order to teach the technical solutions of the present invention, some conventional aspects have been simplified or omitted. Those skilled in the art will appreciate that modifications or substitutions derived from these embodiments will fall within the scope of the present invention. Those skilled in the art will appreciate that the features described below can be combined in various ways to form multiple variations of the invention.

分子筛的吸附分离技术已在医疗、工业等多方面得到应用,分子筛吸附是一个物理过程,分子的偶极距越大,被吸引和吸附的越牢,氮和氧都是四极矩,且氮的四极距比氧大很多,因此,氮原子与阳离子之间的作用力更强,而被优先吸附。因此,分子筛能够利用混合气体中各组分差异来实现分离,分子筛不仅具有选择吸附性,而且其对吸附质的吸附量随吸附压力的变化而变化,当吸附质分压升高时,吸附剂对吸附质的吸附量增大;分压降低时,吸附量减小。本发明实施例将分子筛的特性与燃料电池系统的入堆空气相结合,能够在采用大气空气的基础上更好的利用氮气及氧气的特性,提高燃料电池系统的效率和可靠性。Molecular sieve adsorption and separation technology has been applied in medical, industrial and other fields. Molecular sieve adsorption is a physical process. The larger the dipole moment of the molecule, the stronger the attraction and adsorption. Nitrogen and oxygen are both quadrupole moments, and nitrogen The quadrupole distance is much larger than that of oxygen, so the force between nitrogen atoms and cations is stronger, and it is preferentially adsorbed. Therefore, molecular sieves can use the difference of each component in the mixed gas to achieve separation. Molecular sieves not only have selective adsorption, but also the adsorption capacity of the adsorbate changes with the adsorption pressure. When the partial pressure of the adsorbate increases, the adsorbent The adsorption capacity of the adsorbate increases; when the partial pressure decreases, the adsorption capacity decreases. In the embodiment of the present invention, the characteristics of molecular sieves are combined with the stacking air of the fuel cell system, and the characteristics of nitrogen and oxygen can be better utilized on the basis of using atmospheric air, thereby improving the efficiency and reliability of the fuel cell system.

实施例1Example 1

在本实施例中,提供了一种利用分子筛的燃料电池空气处理系统,参见附图1,所述燃料电池空气处理系统包括与燃料电池电堆1的阴极室入口连接的空气进气管路2,所述空气进气管路2上设置有空滤21、空压机22、中冷器24及分子筛23,所述空滤21、空压机22及中冷器24依次连接,所述分子筛23设置在中冷器24及燃料电池电堆1之间,所述分子筛23还与氮气脱附管路3连接。In this embodiment, a fuel cell air treatment system using molecular sieves is provided, referring to FIG. 1 , the fuel cell air treatment system includes an air intake line 2 connected to the inlet of the cathode chamber of the fuel cell stack 1 , The air intake line 2 is provided with an air filter 21, an air compressor 22, an intercooler 24 and a molecular sieve 23. The air filter 21, the air compressor 22 and the intercooler 24 are connected in sequence, and the molecular sieve 23 is provided with Between the intercooler 24 and the fuel cell stack 1 , the molecular sieve 23 is also connected to the nitrogen desorption pipeline 3 .

通过本实施例结构能够通过空压机的吸附力将氮气吸附在分子筛上,分离氮气后,氧气通过空压机进入到电堆,提高了阴极氧气浓度,进而提高了电堆性能;而且,本实施例中空压机设置在分子筛之前,分子筛与空压机之间添加中冷器,能够使分子筛的工作效率更高,寿命更长。本实施例中,还可以设置干燥机等,用于调节入堆气体湿度。Through the structure of this embodiment, nitrogen can be adsorbed on the molecular sieve by the adsorption force of the air compressor. After the nitrogen is separated, the oxygen enters the stack through the air compressor, which increases the oxygen concentration of the cathode, thereby improving the performance of the stack; In the embodiment, the air compressor is arranged before the molecular sieve, and an intercooler is added between the molecular sieve and the air compressor, which can make the molecular sieve work more efficiently and have a longer life. In this embodiment, a dryer or the like may also be provided to adjust the humidity of the incoming gas.

优选地,所述氮气脱附管路3包括氮气吹扫支路32,所述氮气吹扫支路32的两端分别与分子筛23及燃料电池电堆1的阴极室入口相连通。在吹扫模式下,可以将脱附氮气用于吹扫,实现有效的改善原吹扫方案吹扫气体采用空气,而空气中含有氧气这一不利因素,用氮气吹扫可以有效的提高电堆性能。Preferably, the nitrogen desorption pipeline 3 includes a nitrogen purging branch 32 , and both ends of the nitrogen purging branch 32 are respectively connected to the molecular sieve 23 and the inlet of the cathode chamber of the fuel cell stack 1 . In the purging mode, desorbed nitrogen can be used for purging to achieve effective improvement. The original purging scheme uses air as the purging gas, and the air contains oxygen, which is an unfavorable factor. Using nitrogen purging can effectively improve the stack. performance.

优选地,所述燃料电池空气处理系统还包括空气补充路4,所述空气补充路4的进气口设置在空压机22与中冷器24之间的空气进气管路2,所述空气补充路4的出气口设置在分子筛23与燃料电池电堆1之间的空气进气管路2。空气补充路4能够有效方便的调节空压机输入燃料电池电堆的氧气的浓度,保证氧气浓度可以调节的范围变大,能够适合不同氧气浓度的需求,也可以通过中冷器及空气补充路调节入堆氧气浓度。Preferably, the fuel cell air handling system further includes an air supplementary circuit 4, and the air inlet of the air supplementary circuit 4 is arranged in the air intake pipe 2 between the air compressor 22 and the intercooler 24, and the air The air outlet of the supplementary path 4 is arranged in the air intake line 2 between the molecular sieve 23 and the fuel cell stack 1 . The air supplementary circuit 4 can effectively and conveniently adjust the oxygen concentration of the air compressor input to the fuel cell stack, ensuring that the oxygen concentration can be adjusted in a larger range, and can meet the needs of different oxygen concentrations. Adjust the oxygen concentration into the stack.

优选地,所述分子筛23至少包括第一分子筛及第二分子筛,所述第一分子筛与第二分子筛并联。由于吸附、脱附会有大的压力波动,通过两个分子筛交替使用能够有效避免压力波动,达到压力平衡。进一步地,分子筛也可以设置为多个并联,例如3、4、5或6个等,或者多个串联之后再进行并联,其安装方式可以根据需要合理配置。Preferably, the molecular sieve 23 includes at least a first molecular sieve and a second molecular sieve, and the first molecular sieve and the second molecular sieve are connected in parallel. Due to the large pressure fluctuations in adsorption and desorption, alternating use of two molecular sieves can effectively avoid pressure fluctuations and achieve pressure balance. Further, molecular sieves can also be arranged in parallel, for example, 3, 4, 5, or 6, or a plurality of sieves in series and then connected in parallel, and the installation methods can be reasonably configured as required.

优选地,所述氮气脱附管路3还包括氮气排出支路31,所述氮气排出支路31与大气相连通,所述氮气排出支路31上设置有三通阀。在燃料电池工作模式下,可以同时通过分子筛脱附,分子筛脱附的氮气可以在工作模式下直接排到大气。Preferably, the nitrogen desorption pipeline 3 further includes a nitrogen discharge branch 31 , the nitrogen discharge branch 31 is communicated with the atmosphere, and a three-way valve is provided on the nitrogen discharge branch 31 . In the working mode of the fuel cell, it can be desorbed by the molecular sieve at the same time, and the nitrogen desorbed by the molecular sieve can be directly discharged to the atmosphere in the working mode.

优选地,所述空气补充路4还可以设置阀门,可以根据控制阀门的开度调节不同路径的空气进气量。Preferably, the air supplementary path 4 can also be provided with a valve, and the air intake volume of different paths can be adjusted according to the opening degree of the control valve.

优选地,所述第一分子筛及第二分子筛分别与氮气脱附管路及空压机阀门之间设置阀门。本实施例中能够实现第一分子筛及第二分子筛单独的开闭,第一分子筛可以单独的与空压机连通,也可以单独的与氮气脱附管路连通,当然也可以通过调节阀门开度调节不同分子筛与各个管路的连通关系,例如可以空压机及阀门开度调节第一分子筛及第二分子筛的吸附压力,也可以每个分子筛23设置不同的压力调节结构。优选地,第一分子筛与空压机连通时,第二分子筛与氮气脱附管路连通;第二分子筛与空压机连通时,第一分子筛与氮气脱附管路连通,实现分子筛的交替使用,保证管路中的压力平衡;且能够在燃料电池阴极不间断工作的前提下,在线实现分子筛的氮气吸附、脱附过程,保证分子筛的持续使用。Preferably, valves are respectively arranged between the first molecular sieve and the second molecular sieve and the nitrogen desorption pipeline and the valve of the air compressor. In this embodiment, the first molecular sieve and the second molecular sieve can be opened and closed independently. The first molecular sieve can be connected to the air compressor or the nitrogen desorption pipeline separately. Of course, the opening of the valve can also be adjusted. To adjust the communication relationship between different molecular sieves and each pipeline, for example, the air compressor and valve opening can adjust the adsorption pressure of the first molecular sieve and the second molecular sieve, or each molecular sieve 23 can be provided with different pressure adjustment structures. Preferably, when the first molecular sieve is communicated with the air compressor, the second molecular sieve is communicated with the nitrogen desorption pipeline; when the second molecular sieve is communicated with the air compressor, the first molecular sieve is communicated with the nitrogen desorption pipeline to realize alternate use of molecular sieves , to ensure the pressure balance in the pipeline; and under the premise of uninterrupted operation of the cathode of the fuel cell, the nitrogen adsorption and desorption process of the molecular sieve can be realized online to ensure the continuous use of the molecular sieve.

本实施例还提供一种利用分子筛的燃料电池空气控制方法,首先进行分子筛23的安装,在与燃料电池电堆的阴极室入口连接的空气进气管路2上依次连通空滤21、空压机22、中冷器24及分子筛23,将所述分子筛23设置在空压机22下游,且分子筛上游设置中冷器,即设置在中冷器24与燃料电池电堆1之间;其中分子筛可以存储在存储罐中,也可以存储在袋体中,也可以安装在管路当中,安装方便,成本低。This embodiment also provides a fuel cell air control method using molecular sieves. First, the molecular sieve 23 is installed, and the air intake pipe 2 connected to the inlet of the cathode chamber of the fuel cell stack is connected to the air filter 21 and the air compressor in sequence. 22. Intercooler 24 and molecular sieve 23, the molecular sieve 23 is arranged downstream of the air compressor 22, and an intercooler is arranged upstream of the molecular sieve, that is, between the intercooler 24 and the fuel cell stack 1; the molecular sieve can be It can be stored in a storage tank, can also be stored in a bag body, or can be installed in a pipeline, with convenient installation and low cost.

安装好之后的控制方法包括:利用空压机的吸附力提升空气进气管路的压力,从而提高分子筛的吸附压力,增加分子筛的吸附力,使分子筛吸附分离空气中的氮气,从而得到氧气浓度提升的吸附后空气,空压机再将所述吸附后空气输入燃料电池电堆的阴极室入口,其中,输入电堆的吸附后空气中的氧气浓度高于大气空气中氧气浓度,而且其浓度可以通过控制空压机的参数进行调节。The control method after installation includes: using the adsorption force of the air compressor to increase the pressure of the air intake pipeline, thereby increasing the adsorption pressure of the molecular sieve, increasing the adsorption force of the molecular sieve, so that the molecular sieve adsorbs and separates the nitrogen in the air, so as to obtain an increase in the oxygen concentration. The air after adsorption, the air compressor then inputs the air after adsorption into the inlet of the cathode chamber of the fuel cell stack, wherein the concentration of oxygen in the air after adsorption into the stack is higher than the concentration of oxygen in atmospheric air, and its concentration can be Adjust by controlling the parameters of the air compressor.

优选地,为了保证压力平衡,使系统更稳定,可以将分子筛设置为并联的第一分子筛与第二分子筛,交替使用所述第一分子筛与第二分子筛实现氮气吸附及脱附过程的压力平衡;例如,当第一分子筛吸附到一定程度时,进行分子筛的交替,使第二分子筛处于燃料电池工作模式下进行氮气吸附,而第一分子筛进行氮气脱附,如此反复交替使用,实现燃料电池的平稳运行。Preferably, in order to ensure the pressure balance and make the system more stable, the molecular sieve can be set as the first molecular sieve and the second molecular sieve in parallel, and the first molecular sieve and the second molecular sieve are alternately used to achieve the pressure balance in the nitrogen adsorption and desorption process; For example, when the first molecular sieve is adsorbed to a certain extent, alternate molecular sieves, so that the second molecular sieve is in the fuel cell working mode for nitrogen adsorption, while the first molecular sieve is used for nitrogen desorption. run.

优选地,为了更有利于入口气体中氧气浓度的调节,及扩大调节的范围,还在空压机下游设置空气补充路,所述空气补充路的进气口设置在空压机与中冷器之间的空气进气管路,所述空气补充路的出气口设置在分子筛与燃料电池电堆之间的空气进气管路,通过空气补充路调节进入燃料电池电堆的氧气浓度。也可以通过中冷器进行调节。Preferably, in order to be more conducive to the adjustment of the oxygen concentration in the inlet gas, and to expand the adjustment range, an air supplementary circuit is also arranged downstream of the air compressor, and the air inlet of the air supplementary circuit is provided at the air compressor and the intercooler. The air intake pipeline between the air supply pipelines, the air outlet of the air supplementary pipeline is arranged in the air intake pipeline between the molecular sieve and the fuel cell stack, and the oxygen concentration entering the fuel cell stack is adjusted through the air supplementary pipeline. It can also be adjusted via an intercooler.

优选地,可以通过空压机和其他设备降低分子筛的吸附压力,实现脱附分子筛吸附的氮气;脱附的氮气输入氮气脱附管路,在燃料电池工作模式将氮气通过氮气脱附管路的氮气排出支路排出至大气;在燃料电池吹扫模式将氮气通过氮气脱附管路的氮气吹扫支路输入燃料电池电堆的阴极室入口。Preferably, the adsorption pressure of the molecular sieve can be reduced by an air compressor and other equipment to realize the desorption of nitrogen adsorbed by the molecular sieve; the desorbed nitrogen is input into the nitrogen desorption pipeline, and the nitrogen is passed through the nitrogen desorption pipeline in the working mode of the fuel cell. The nitrogen discharge branch is discharged to the atmosphere; in the fuel cell purging mode, nitrogen is input into the cathode chamber inlet of the fuel cell stack through the nitrogen purging branch of the nitrogen desorption pipeline.

优选地,如图2所示,提供一种利用分子筛的燃料电池空气控制方法,包括:Preferably, as shown in FIG. 2, a fuel cell air control method using molecular sieve is provided, comprising:

S101启动燃料电池电堆,开启燃料电池空气处理系统中氮气排出支路的阀门;S101 starts the fuel cell stack, and opens the valve of the nitrogen discharge branch in the fuel cell air handling system;

S102根据燃料电池电堆性能确定入堆的氧气浓度目标需求;S102 determines the target requirement of oxygen concentration into the stack according to the performance of the fuel cell stack;

S103通过控制阀门开度分配空气进气管路进入中冷器与空气补充路的空气流量;S103 distributes the air flow of the air intake pipe into the intercooler and the air supplementary circuit by controlling the valve opening;

S104按照预设条件控制第一分子筛及第二分子筛与空压机交替连通;S104 controls the first molecular sieve and the second molecular sieve to alternately communicate with the air compressor according to preset conditions;

S105判断是否到达吹扫时机,若是,则转至S106;若否,则转至S104;S105 judges whether the purging timing is reached, if so, go to S106; if not, go to S104;

S106关闭燃料电池空气处理系统中氮气排出支路的阀门;S106 closes the valve of the nitrogen discharge branch in the fuel cell air handling system;

S107降低空压机转速,减小空压机下游的阀门的开度;S107 Reduce the speed of the air compressor and reduce the opening of the valve downstream of the air compressor;

S108确定吹扫结束,关机。In S108, it is determined that the purging is completed, and the power is turned off.

本实施例中,在空气进气管路中将分子筛设置在空压机的下游游,分子筛与空压机之间添加中冷器,还可以添加干燥机等,利用空压机增加其中一分子筛的吸附压力,实现了分子筛大量自动的吸附空气中的氮气;空压机将分子筛吸附后的空气(氧气浓度高)输入燃料电池电堆的阴极室入口;在S101中,可以设置不同的管路,通过控制阀门将经过分子筛的气体匹配进入空压机或排至大气;在S102中,根据电堆性能需要,预先计算提高多少氧气浓度能够对应提高多少电堆性能,在S103中根据预设的目标进行流量的分配,其中,进入中冷器的高温高压气体通过中冷器进行降温后再通过分子筛,可以增加分子筛的使用寿命,分子筛进行氮气的吸附,输出的气体为高浓度的氧气,其氧气浓度可以通过计算或实验获得,通过空气补充路的气体为大气中的空气,其中氧气浓度可知,可以根据预设的氧的浓度需求,分别计算不同管路的气体流量,再根据流量分配阀门开度;在S104步骤中,预设条件可以是预设时间,例如当到达1小时后,切换分子筛阀门,将吸附中的分子筛与氮气排出支路连通,另一分子筛,即脱附后的分子筛与空压机连通,进行交替使用,与氮气排出支路连通的分子筛,由于吸附压力降低,分子筛吸附的氮气自动脱附,并通过氮气脱附管路排出至大气。即分子筛在减压时将吸附的氮气从分子筛脱附下来,排放回环境空气中,再下一次加压时又可以重新吸附氮气从而提升氧气浓度,整个过程形成周期性的动态循环过程;在S106、S107中,在燃料电池吹扫模式下,能够根据吹扫流量需求,利用分子筛脱附的氮气进行吹扫,通过氮气脱附管路的氮气吹扫支路输入燃料电池电堆的阴极室入口,从而避免吹扫中残留氧;其中,缓慢降低空压机转速,及减小空压机下游的阀门的开度,能够避免空压机喘振等现象,保证氮气吹扫过程更稳定。In this embodiment, the molecular sieve is arranged downstream of the air compressor in the air intake pipeline, an intercooler is added between the molecular sieve and the air compressor, and a dryer can also be added, and the air compressor is used to increase the size of one of the molecular sieves. The adsorption pressure enables the molecular sieve to automatically absorb a large amount of nitrogen in the air; the air compressor feeds the air (with high oxygen concentration) adsorbed by the molecular sieve into the inlet of the cathode chamber of the fuel cell stack; in S101, different pipelines can be set, By controlling the valve, the gas passing through the molecular sieve is matched into the air compressor or discharged to the atmosphere; in S102, according to the performance requirements of the stack, it is pre-calculated how much oxygen concentration can be improved corresponding to how much the stack performance can be improved, and in S103 according to the preset target The flow distribution is carried out. Among them, the high temperature and high pressure gas entering the intercooler is cooled by the intercooler and then passed through the molecular sieve, which can increase the service life of the molecular sieve. The molecular sieve performs nitrogen adsorption, and the output gas is high-concentration oxygen. The concentration can be obtained by calculation or experiment. The gas passing through the air supplementary path is the air in the atmosphere, and the oxygen concentration can be known. According to the preset oxygen concentration requirement, the gas flow of different pipelines can be calculated separately, and then the valve is opened according to the flow distribution. In step S104, the preset condition can be a preset time, for example, when it reaches 1 hour, switch the molecular sieve valve, connect the molecular sieve in adsorption with the nitrogen discharge branch, and the other molecular sieve, that is, the molecular sieve after desorption and The air compressor is connected and used alternately. The molecular sieve connected with the nitrogen discharge branch will automatically desorb the nitrogen adsorbed by the molecular sieve due to the decrease of the adsorption pressure, and will be discharged to the atmosphere through the nitrogen desorption pipeline. That is, the molecular sieve desorbs the adsorbed nitrogen from the molecular sieve during decompression, and discharges it back into the ambient air. When the next pressurization is performed, nitrogen can be re-adsorbed to increase the oxygen concentration. The whole process forms a periodic dynamic cycle process; in S106 . In S107, in the fuel cell purge mode, the nitrogen desorbed from the molecular sieve can be used for purging according to the purge flow requirement, and the nitrogen purge branch of the nitrogen desorption pipeline is input to the inlet of the cathode chamber of the fuel cell stack. , so as to avoid residual oxygen in the purging; among them, slowly reducing the speed of the air compressor and reducing the opening of the valve downstream of the air compressor can avoid the phenomenon of air compressor surge and ensure that the nitrogen purging process is more stable.

基于同一发明构思,本实施例还提供了一种燃料电池系统、车辆,由于该燃料电池系统、车辆所解决问题的原理与前述实施例的一种利用分子筛的燃料电池空气处理系统相似,因此本实施例的实施可以参见前述一种利用分子筛的燃料电池空气处理系统的实施,重复之处不再赘述。Based on the same inventive concept, the present embodiment also provides a fuel cell system and a vehicle. Since the principle of the problem solved by the fuel cell system and the vehicle is similar to the fuel cell air treatment system using molecular sieves in the foregoing embodiments, the present embodiment For the implementation of the embodiment, reference may be made to the implementation of the aforementioned fuel cell air treatment system using molecular sieves, and repeated details will not be repeated.

本发明实施例还提供了一种燃料电池系统,包括燃料电池电堆,所述燃料电池电堆的阴极室入口与上述任意一实施例所述的利用分子筛的燃料电池空气处理系统的空气进气管路相连通。本实施例的燃料电池系统能够调节氧气的浓度,具有较高的效率和可靠性。An embodiment of the present invention further provides a fuel cell system, including a fuel cell stack, the inlet of the cathode chamber of the fuel cell stack and the air intake pipe of the fuel cell air treatment system using molecular sieve described in any one of the above embodiments The road is connected. The fuel cell system of this embodiment can adjust the concentration of oxygen and has high efficiency and reliability.

本发明实施例还提供了一种车辆,所述车辆包括如上任意实施例所述的燃料电池系统。Embodiments of the present invention also provide a vehicle, the vehicle including the fuel cell system described in any of the above embodiments.

实施例2Example 2

基于与实施例1同一发明构思,本实施例提供一种利用分子筛的低尾排燃料电池空气处理系统,参考附图3,包括与燃料电池电堆1阴极室入口连接的空气进气管路2,所述空气进气管路2上设置有空滤21、空压机22、中冷器24及分子筛23,所述空滤21、空压机22及中冷器24依次连接,所述分子筛23设置在中冷器24及燃料电池电堆1之间,所述分子筛23还与氮气脱附管路3连接,所述氮气脱附管路3上设置有氮气尾排支路33,所述氮气尾排支路33与燃料电池电堆的氢气尾排管路5相连通。本实施例中,分子筛与空压机之间添加中冷器和干燥机等,不仅能够提高氧气浓度,还能够利用分子筛出来的氮气通过氮气尾排支路降低尾排氢浓度,中冷器还可以通过空气补充路调节入堆氧气浓度。Based on the same inventive concept as in Embodiment 1, this embodiment provides a low tail-emission fuel cell air treatment system using molecular sieves. Referring to FIG. 3 , it includes an air intake line 2 connected to the inlet of the cathode chamber of the fuel cell stack 1 , The air intake line 2 is provided with an air filter 21, an air compressor 22, an intercooler 24 and a molecular sieve 23. The air filter 21, the air compressor 22 and the intercooler 24 are connected in sequence, and the molecular sieve 23 is provided with Between the intercooler 24 and the fuel cell stack 1, the molecular sieve 23 is also connected to the nitrogen desorption pipeline 3, and the nitrogen desorption pipeline 3 is provided with a nitrogen tail exhaust branch 33, and the nitrogen tail The exhaust branch 33 communicates with the hydrogen tail exhaust pipeline 5 of the fuel cell stack. In this embodiment, adding an intercooler and a dryer between the molecular sieve and the air compressor can not only increase the oxygen concentration, but also use the nitrogen from the molecular sieve to reduce the hydrogen concentration in the tail exhaust through the nitrogen tail exhaust branch. The intercooler also The oxygen concentration in the stack can be adjusted through the air supplementary circuit.

优选地,所述氮气脱附管路3包括氮气吹扫支路32,所述氮气吹扫支路32的两端分别与分子筛23及燃料电池电堆1的阴极室入口相连通。在吹扫模式下,可以将脱附氮气用于吹扫,实现有效的改善原吹扫方案吹扫气体采用空气,而空气中含有氧气这一不利因素,用氮气吹扫可以有效的提高电堆性能。Preferably, the nitrogen desorption pipeline 3 includes a nitrogen purging branch 32 , and both ends of the nitrogen purging branch 32 are respectively connected to the molecular sieve 23 and the inlet of the cathode chamber of the fuel cell stack 1 . In the purging mode, desorbed nitrogen can be used for purging to achieve effective improvement. The original purging scheme uses air as the purging gas, and the air contains oxygen, which is an unfavorable factor. Using nitrogen purging can effectively improve the stack. performance.

优选地,所述低尾排燃料电池空气处理系统还包括空气补充路4,所述空气补充路4的进气口设置在空压机22与中冷器24之间的空气进气管路2,所述空气补充路4的出气口设置在分子筛23与燃料电池电堆1之间的空气进气管路2;空气补充路4将空压机出口空气直接引入电堆能够更有效方便的调节入燃料电池电堆的氧气的浓度,保证氧气浓度可以调节的范围变大,能够适合不同氧气浓度的需求。Preferably, the low tail exhaust fuel cell air treatment system further includes an air supplementary circuit 4, and the air inlet of the air supplementary circuit 4 is arranged in the air intake line 2 between the air compressor 22 and the intercooler 24, The air outlet of the air supplementary circuit 4 is arranged in the air intake line 2 between the molecular sieve 23 and the fuel cell stack 1; the air supplementary circuit 4 directly introduces the air from the air compressor outlet into the stack, which can more effectively and conveniently adjust the fuel input. The oxygen concentration of the battery stack ensures that the range in which the oxygen concentration can be adjusted becomes larger, which can meet the needs of different oxygen concentrations.

优选地,所述低尾排燃料电池空气处理系统还包括空气补充路4及增湿器25,所述增湿器5设置分子筛23与燃料电池电堆1之间,所述空气补充路4的进气口设置在空压机22与中冷器24之间的空气进气管路2,所述空气补充路4的出气口设置在分子筛23与增湿器25之间的空气进气管路2。本实施例中在分子筛后面设置增湿器可以直接提高入堆氧气湿度。Preferably, the low tail exhaust fuel cell air treatment system further includes an air supplementary circuit 4 and a humidifier 25, the humidifier 5 is arranged between the molecular sieve 23 and the fuel cell stack 1, and the air supplementary circuit 4 The air inlet is provided in the air intake line 2 between the air compressor 22 and the intercooler 24 , and the air outlet of the air supplementary line 4 is provided in the air intake line 2 between the molecular sieve 23 and the humidifier 25 . In this embodiment, setting a humidifier behind the molecular sieve can directly increase the humidity of the incoming oxygen.

优选地,所述分子筛23至少包括第一分子筛及第二分子筛,所述第一分子筛与第二分子筛并联。由于吸附、脱附会有大的压力波动,通过两个分子筛交替使用能够有效避免压力波动,达到压力平衡。进一步地,分子筛也可以设置为多个并联,或者多个串联之后再进行并联,其安装方式可以根据需要合理配置。Preferably, the molecular sieve 23 includes at least a first molecular sieve and a second molecular sieve, and the first molecular sieve and the second molecular sieve are connected in parallel. Due to the large pressure fluctuations in adsorption and desorption, alternating use of two molecular sieves can effectively avoid pressure fluctuations and achieve pressure balance. Further, the molecular sieves can also be set up in parallel, or in parallel after a plurality of series, and the installation method can be reasonably configured as required.

优选地,为了方便控制,例如吹扫模式及正常工作模式的切换,可以分别在氮气脱附管路3、氮气尾排支路33、所述氮气吹扫支路32上设置有三通阀,可以每个管路均安装对应阀门,也可以在其中一个管路上设置一个三通阀。在燃料电池工作模式下,可以同时进行分子筛脱附,分子筛脱附的氮气通过燃料电池电堆的氢气尾排管路输出,从而降低氢气的浓度,提升安全性能。Preferably, in order to facilitate control, such as switching between the purging mode and the normal working mode, a three-way valve may be provided on the nitrogen desorption pipeline 3, the nitrogen tail exhaust branch 33, and the nitrogen purging branch 32, respectively. Each pipeline is equipped with a corresponding valve, or a three-way valve can be set on one of the pipelines. In the fuel cell working mode, the molecular sieve desorption can be carried out at the same time, and the nitrogen desorbed by the molecular sieve is output through the hydrogen tailpipe of the fuel cell stack, thereby reducing the concentration of hydrogen and improving the safety performance.

本实施例还提供一种利用分子筛的低尾排燃料电池空气控制方法,首先,将与燃料电池电堆的阴极室入口连接的空气进气管路上的空滤、空压机中冷器及分子筛依次连接,将所述分子筛设置在中冷器与燃料电池电堆之间;设置所述分子筛的氮气脱附管路,并将其中氮气脱附管路的氮气尾排支路与燃料电池电堆的氢气尾排管路的相连通,使脱附的氮气通过氢气尾排管路排除。This embodiment also provides an air control method for a low tail exhaust fuel cell using molecular sieves. First, the air filter on the air intake pipeline connected to the inlet of the cathode chamber of the fuel cell stack, the air compressor intercooler and the molecular sieve are sequentially connected. Connect the molecular sieve between the intercooler and the fuel cell stack; set the nitrogen desorption pipeline of the molecular sieve, and connect the nitrogen tail exhaust branch of the nitrogen desorption pipeline to the fuel cell stack. The hydrogen tail exhaust pipeline is connected, so that the desorbed nitrogen is discharged through the hydrogen tail exhaust pipeline.

安装好之后的处理流程包括:通过空压机的吸附力增加分子筛的吸附压力,分子筛吸附空气中的氮气,使氮气从空气中分离,分离得到吸附后空气,吸附后空气中的氧气浓度较高,空压机将所述吸附后空气输入燃料电池电堆的阴极室入口;保证入堆的氧气浓度升高且能够控制;当降低分子筛的吸附压力时,分子筛脱附吸附的氮气,将所述脱附的氮气通过氮气脱附管路上设置的氮气尾排支路输入燃料电池电堆的氢气尾排管路。The treatment process after installation includes: increasing the adsorption pressure of the molecular sieve by the adsorption force of the air compressor, the molecular sieve adsorbs the nitrogen in the air, separates the nitrogen from the air, and separates the adsorbed air, and the oxygen concentration in the air after adsorption is high. , the air compressor will input the adsorbed air into the inlet of the cathode chamber of the fuel cell stack; ensure that the oxygen concentration in the stack is increased and can be controlled; when the adsorption pressure of the molecular sieve is reduced, the molecular sieve will desorb the adsorbed nitrogen, and the The desorbed nitrogen is fed into the hydrogen tailpipe of the fuel cell stack through the nitrogen tailpipe branch provided on the nitrogen desorption pipeline.

优选地,为了保证压力平衡,使系统更稳定,可以将分子筛设置为并联的第一分子筛与第二分子筛,交替使用所述第一分子筛与第二分子筛实现氮气吸附及脱附过程的压力平衡;例如,当第一分子筛吸附到一定程度时,进行分子筛的交替,使第二分子筛处于燃料电池工作模式下进行氮气吸附,而第一分子筛进行氮气脱附,如此反复交替使用,实现燃料电池的平稳运行。Preferably, in order to ensure the pressure balance and make the system more stable, the molecular sieve can be set as the first molecular sieve and the second molecular sieve in parallel, and the first molecular sieve and the second molecular sieve are alternately used to achieve the pressure balance in the nitrogen adsorption and desorption process; For example, when the first molecular sieve is adsorbed to a certain extent, alternate molecular sieves, so that the second molecular sieve is in the fuel cell working mode for nitrogen adsorption, while the first molecular sieve is used for nitrogen desorption. run.

优选地,为了更有利于入口气体中氧气浓度的调节,及扩大调节的范围,在燃料电池电堆与分子筛之间设置空气补充路及增湿器,将所述增湿器设置在分子筛与电堆之间,所述空气补充路的进气口设置在空压机与中冷器之间的空气进气管路,所述空气补充路的出气口设置在分子筛与增湿器之间的空气进气管路。Preferably, in order to be more conducive to the adjustment of the oxygen concentration in the inlet gas and to expand the adjustment range, an air supplementary circuit and a humidifier are arranged between the fuel cell stack and the molecular sieve, and the humidifier is arranged between the molecular sieve and the electric sieve. Between the stacks, the air inlet of the air supplementary path is arranged in the air inlet line between the air compressor and the intercooler, and the air outlet of the air supplementary path is arranged in the air inlet between the molecular sieve and the humidifier. Air line.

通过空气补充路调节进入燃料电池电堆的氧气浓度。The oxygen concentration entering the fuel cell stack is regulated by an air make-up circuit.

优选地,可以通过空压机和其他设备降低分子筛的吸附压力,实现脱附分子筛吸附的氮气;脱附的氮气输入氮气脱附管路,在燃料电池工作模式将氮气通过氮气脱附管路的氮气尾排支路输入氢气尾排管路排出;在燃料电池吹扫模式将氮气通过氮气脱附管路的氮气吹扫支路输入燃料电池电堆的阴极室入口。Preferably, the adsorption pressure of the molecular sieve can be reduced by an air compressor and other equipment to realize the desorption of nitrogen adsorbed by the molecular sieve; the desorbed nitrogen is input into the nitrogen desorption pipeline, and the nitrogen is passed through the nitrogen desorption pipeline in the working mode of the fuel cell. The nitrogen tail exhaust branch is input into the hydrogen tail exhaust pipe and discharged; in the fuel cell purging mode, nitrogen is input into the cathode chamber inlet of the fuel cell stack through the nitrogen purging branch of the nitrogen desorption pipeline.

优选地,如图4所示,提供一种利用分子筛的低尾排燃料电池空气控制方法,包括:Preferably, as shown in FIG. 4 , a method for controlling air in a low tail exhaust fuel cell using molecular sieves is provided, including:

S201启动燃料电池电堆,开启低尾排燃料电池空气处理系统中氮气排出支路的阀门;S201 starts the fuel cell stack, and opens the valve of the nitrogen discharge branch in the low tail exhaust fuel cell air handling system;

S202根据燃料电池电堆性能确定入堆的氧气浓度目标需求;S202 determines the target requirement of oxygen concentration into the stack according to the performance of the fuel cell stack;

S203通过控制阀门开度分配空气进气管路进入中冷器与空气补充路的空气流量;S203 distributes the air flow of the air intake pipe into the intercooler and the air supplementary circuit by controlling the valve opening;

S204将脱附后的氮气通过氢气尾排管路排出;S204 discharges the desorbed nitrogen through the hydrogen tailpipe;

S205按照预设条件控制第一分子筛及第二分子筛与空压机交替连通;S205 controls the first molecular sieve and the second molecular sieve to communicate alternately with the air compressor according to preset conditions;

S206判断是否到达吹扫时机,若是,则转至S207;若否,则转至S205;S206 judges whether the purging timing is reached, if so, go to S207; if not, go to S205;

S207关闭低尾排燃料电池空气处理系统中氮气排出支路的阀门;S207 Close the valve of the nitrogen discharge branch in the low tail exhaust fuel cell air handling system;

S208降低空压机转速,减小空压机下游的阀门的开度;S208 reduces the speed of the air compressor and reduces the opening of the valve downstream of the air compressor;

S209确定吹扫结束,关机。S209 determines that the purging is over, and shuts down.

本实施例中,分子筛吸附的氮气可以由于降低压力,自行脱附,也可以通过外接的降低压力或其他方式实现脱附,脱附的氮气通过氮气脱附管路上设置的氮气尾排支路输入燃料电池电堆的氢气尾排管路,从而实现减少尾排中氢的浓度。其中在S206到达吹扫时机为燃料电池电堆在要关机状态下,需要避免电堆中含有水存留,影响性能;在S209确定吹扫结束的时机根据燃料电池系统计算不会有水存留或结冰。In this embodiment, the nitrogen adsorbed by the molecular sieve can be desorbed by itself by reducing the pressure, or it can be desorbed by an external pressure reduction or other methods. The desorbed nitrogen is input through the nitrogen tail exhaust branch set on the nitrogen desorption pipeline. The hydrogen tailpipe of the fuel cell stack can reduce the concentration of hydrogen in the tailpipe. The purging timing in S206 is that the fuel cell stack is in the shutdown state, and it is necessary to avoid water retention in the stack, which will affect the performance; in S209, the timing for the end of purging is determined according to the fuel cell system. ice.

基于同一发明构思,本实施例还提供了一种燃料电池系统、车辆,由于该燃料电池系统、车辆所解决问题的原理与前述实施例的一种利用分子筛的低尾排燃料电池空气处理系统相似,因此本实施例的实施可以参见前述一种利用分子筛的低尾排燃料电池空气处理系统的实施,重复之处不再赘述。Based on the same inventive concept, the present embodiment also provides a fuel cell system and a vehicle, because the principle of the problem solved by the fuel cell system and the vehicle is similar to the low tail exhaust fuel cell air treatment system using molecular sieves in the foregoing embodiment Therefore, for the implementation of this embodiment, reference may be made to the implementation of the aforementioned low-tail exhaust fuel cell air treatment system using molecular sieves, and repeated details will not be repeated.

本发明实施例还提供了一种燃料电池系统,包括燃料电池电堆,所述燃料电池电堆的阴极室入口与上述任意一实施例所述的利用分子筛的低尾排燃料电池空气处理系统的空气进气管路相连通。本实施例的燃料电池系统能够调节氧气的浓度,具有较高的效率和可靠性,其能够有效降低氢气排放的浓度。An embodiment of the present invention further provides a fuel cell system, including a fuel cell stack, the inlet of the cathode chamber of the fuel cell stack is connected to the air treatment system of the low tail exhaust fuel cell air treatment system using molecular sieve according to any one of the above embodiments. The air intake lines are connected. The fuel cell system of this embodiment can adjust the concentration of oxygen, has high efficiency and reliability, and can effectively reduce the concentration of hydrogen emissions.

本发明实施例还提供了一种车辆,所述车辆包括如上任意实施例所述的燃料电池系统。Embodiments of the present invention also provide a vehicle, the vehicle including the fuel cell system described in any of the above embodiments.

实施例3Example 3

基于与实施例1同一发明构思,本实施例提供一种利用分子筛的氧气循环燃料电池空气处理系统,参考附图5,包括与燃料电池电堆1阴极室入口连接的空气进气管路2,及与燃料电池电堆的阴极室出口连接的空气出气管路,所述空气进气管路2上设置有空滤21、空压机22、中冷器24及分子筛23,所述空滤21、空压机22及中冷器24依次连接,所述分子筛23设置在中冷器24及燃料电池电堆1之间,所述分子筛23还设置有与氮气脱附管路3连接的脱气口,所述空气出气管路的出口与空压机下游的空气进气管路相连通形成氧气循环管路6。在本实施例中,提高氧气浓度的同时,还能够通过设计的氧气循环管路更有效的利用氧气,将电堆的氧气湿度引入电堆,从而增加入堆气体增湿。其中氧气循环路可以用氧气循环泵或者引射器等设备更有效的利用了氧气的循环,提高氧气利用率。Based on the same inventive concept as Embodiment 1, this embodiment provides an oxygen cycle fuel cell air treatment system using molecular sieves. Referring to FIG. 5 , it includes an air intake line 2 connected to the inlet of the cathode chamber of the fuel cell stack 1 , and The air outlet pipeline connected to the outlet of the cathode chamber of the fuel cell stack, the air inlet pipeline 2 is provided with an air filter 21, an air compressor 22, an intercooler 24 and a molecular sieve 23. The compressor 22 and the intercooler 24 are connected in sequence, the molecular sieve 23 is arranged between the intercooler 24 and the fuel cell stack 1, and the molecular sieve 23 is also provided with a degassing port connected to the nitrogen desorption pipeline 3, so The outlet of the air outlet pipeline is connected with the air intake pipeline downstream of the air compressor to form an oxygen circulation pipeline 6 . In this embodiment, while increasing the oxygen concentration, oxygen can be used more effectively through the designed oxygen circulation pipeline, and the oxygen humidity of the stack can be introduced into the stack, thereby increasing the humidification of the gas entering the stack. Among them, the oxygen circulation circuit can use the oxygen circulation pump or the ejector and other equipment to make more effective use of the oxygen circulation and improve the oxygen utilization rate.

优选地,所述氮气脱附管路3包括氮气吹扫支路32,所述氮气吹扫支路32的两端分别与分子筛23及燃料电池电堆1的阴极室入口相连通。在吹扫模式下,可以将脱附氮气用于吹扫,实现有效的改善原吹扫方案吹扫气体采用空气,而空气中含有氧气这一不利因素,用氮气吹扫可以有效的提高电堆性能。Preferably, the nitrogen desorption pipeline 3 includes a nitrogen purging branch 32 , and both ends of the nitrogen purging branch 32 are respectively connected to the molecular sieve 23 and the inlet of the cathode chamber of the fuel cell stack 1 . In the purging mode, desorbed nitrogen can be used for purging to achieve effective improvement. The original purging scheme uses air as the purging gas, and the air contains oxygen, which is an unfavorable factor. Using nitrogen purging can effectively improve the stack. performance.

优选地,所述氮气脱附管路3包括氮气尾排支路33,所述氮气尾排支路33的两端分别与分子筛23及燃料电池电堆1的氢气尾排管路5相连通。在正常工作模式下,可以利用分子筛出来的氮气通过氮气尾排支路33降低尾排氢浓度。Preferably, the nitrogen desorption pipeline 3 includes a nitrogen tail exhaust branch 33 , and both ends of the nitrogen exhaust branch 33 are respectively connected with the molecular sieve 23 and the hydrogen exhaust pipeline 5 of the fuel cell stack 1 . In the normal working mode, the nitrogen gas from the molecular sieve can be used to reduce the hydrogen concentration in the tail exhaust through the nitrogen exhaust branch 33 .

优选地,所述低尾排燃料电池空气处理系统还包括空气补充路4,所述空气补充路4的进气口设置在空压机22与中冷器24之间的空气进气管路2,所述空气补充路4的出气口设置在分子筛23与燃料电池电堆1之间的空气进气管路2;空气补充路4将空压机出口高压空气直接引入电堆能够更有效方便的调节入燃料电池电堆的氧气的浓度,保证氧气浓度可以调节的范围变大,能够适合不同氧气浓度的需求。Preferably, the low tail exhaust fuel cell air treatment system further includes an air supplementary circuit 4, and the air inlet of the air supplementary circuit 4 is arranged in the air intake line 2 between the air compressor 22 and the intercooler 24, The air outlet of the air supplementary circuit 4 is arranged in the air intake pipeline 2 between the molecular sieve 23 and the fuel cell stack 1; the air supplementary circuit 4 directly introduces the high-pressure air from the air compressor outlet into the stack, which can more effectively and conveniently adjust the air intake. The oxygen concentration of the fuel cell stack ensures that the adjustable range of the oxygen concentration becomes larger, which can meet the needs of different oxygen concentrations.

优选地,所述低尾排燃料电池空气处理系统还包括空气补充路4及增湿器25,所述增湿器5设置分子筛23与燃料电池电堆1之间,所述空气补充路4的进气口设置在空压机22与中冷器24之间的空气进气管路2,所述空气补充路4的出气口设置在分子筛23与增湿器25之间的空气进气管路2。Preferably, the low tail exhaust fuel cell air treatment system further includes an air supplementary circuit 4 and a humidifier 25, the humidifier 5 is arranged between the molecular sieve 23 and the fuel cell stack 1, and the air supplementary circuit 4 The air inlet is provided in the air intake line 2 between the air compressor 22 and the intercooler 24 , and the air outlet of the air supplementary line 4 is provided in the air intake line 2 between the molecular sieve 23 and the humidifier 25 .

优选地,所述分子筛23至少包括第一分子筛及第二分子筛,所述第一分子筛与第二分子筛并联。由于吸附、脱附会有大的压力波动,通过两个分子筛交替使用能够有效避免压力波动,达到压力平衡。进一步地,分子筛也可以设置为多个并联,或者多个串联之后再进行并联,其安装方式可以根据需要合理配置。Preferably, the molecular sieve 23 includes at least a first molecular sieve and a second molecular sieve, and the first molecular sieve and the second molecular sieve are connected in parallel. Due to the large pressure fluctuations in adsorption and desorption, alternating use of two molecular sieves can effectively avoid pressure fluctuations and achieve pressure balance. Further, the molecular sieves can also be set up in parallel, or in parallel after a plurality of series, and the installation method can be reasonably configured as required.

优选地,为了方便控制,例如吹扫模式及正常工作模式的切换,可以分别在氮气脱附管路3、氮气尾排支路33、所述氮气吹扫支路32上设置有三通阀,可以每个管路均安装对应阀门,也可以在其中一个管路上设置一个三通阀。在燃料电池工作模式下,可以同时进行分子筛脱附,分子筛脱附的氮气通过燃料电池电堆的氢气尾排管路输出,从而降低氢气的浓度,提升安全性能。Preferably, in order to facilitate control, such as switching between the purging mode and the normal working mode, a three-way valve may be provided on the nitrogen desorption pipeline 3, the nitrogen tail exhaust branch 33, and the nitrogen purging branch 32, respectively. Each pipeline is equipped with a corresponding valve, or a three-way valve can be set on one of the pipelines. In the fuel cell working mode, the molecular sieve desorption can be carried out at the same time, and the nitrogen desorbed by the molecular sieve is output through the hydrogen tailpipe of the fuel cell stack, thereby reducing the concentration of hydrogen and improving the safety performance.

本实施例还提供一种利用分子筛的氧气循环燃料电池空气控制方法,首先,将与燃料电池电堆的阴极室入口连接的空气进气管路上的空滤、空压机中冷器及分子筛依次连接,将所述分子筛设置在中冷器与燃料电池电堆之间;设置所述分子筛的氮气脱附管路,并将燃料电池电堆的空气出气管路与设置在所述空压机下游的空气进气管路连通形成氧气循环管路6。This embodiment also provides an oxygen circulation fuel cell air control method using molecular sieves. First, the air filter, the air compressor intercooler and the molecular sieve on the air intake pipeline connected to the inlet of the cathode chamber of the fuel cell stack are sequentially connected , the molecular sieve is arranged between the intercooler and the fuel cell stack; the nitrogen desorption pipeline of the molecular sieve is set, and the air outlet pipeline of the fuel cell stack is connected with the air outlet pipeline arranged downstream of the air compressor. The air intake pipeline is connected to form an oxygen circulation pipeline 6 .

安装好之后的处理流程包括:通过空压机的吸附力增加分子筛的吸附压力,分子筛吸附空气中的氮气,使氮气从空气中分离,分离得到吸附后空气,吸附后空气中的氧气浓度较高,空压机将所述吸附后空气输入燃料电池电堆的阴极室入口,且燃料电池的空气出气管路与空气进气管路连通形成氧气循环管路,氧气循环管路将从电堆排出的湿度较高的氧气带入进气管路,从而提高进入电堆的气体湿度,能够有效为入电堆气体增湿;保证入堆的氧气浓度升高且能够控制;当降低分子筛的吸附压力时,分子筛脱附吸附的氮气,将所述脱附的氮气通过氮气脱附管路排除。The treatment process after installation includes: increasing the adsorption pressure of the molecular sieve by the adsorption force of the air compressor, the molecular sieve adsorbs the nitrogen in the air, separates the nitrogen from the air, and separates the adsorbed air, and the oxygen concentration in the air after adsorption is high. , the air compressor feeds the adsorbed air into the inlet of the cathode chamber of the fuel cell stack, and the air outlet pipeline of the fuel cell is connected with the air inlet pipeline to form an oxygen circulation pipeline, which will be discharged from the stack. Oxygen with high humidity is brought into the intake pipeline, thereby increasing the humidity of the gas entering the stack, which can effectively humidify the gas entering the stack; ensure that the oxygen concentration entering the stack is increased and can be controlled; when the adsorption pressure of the molecular sieve is reduced, The molecular sieve desorbs the adsorbed nitrogen, and the desorbed nitrogen is removed through the nitrogen desorption pipeline.

优选地,为了保证压力平衡,使系统更稳定,可以将分子筛设置为并联的第一分子筛与第二分子筛,交替使用所述第一分子筛与第二分子筛实现氮气吸附及脱附过程的压力平衡;例如,当第一分子筛吸附到一定程度时,进行分子筛的交替,使第二分子筛处于燃料电池工作模式下进行氮气吸附,而第一分子筛进行氮气脱附,如此反复交替使用,实现燃料电池的平稳运行。Preferably, in order to ensure the pressure balance and make the system more stable, the molecular sieve can be set as the first molecular sieve and the second molecular sieve in parallel, and the first molecular sieve and the second molecular sieve are alternately used to achieve the pressure balance in the nitrogen adsorption and desorption process; For example, when the first molecular sieve is adsorbed to a certain extent, alternate molecular sieves, so that the second molecular sieve is in the fuel cell working mode for nitrogen adsorption, while the first molecular sieve is used for nitrogen desorption. run.

优选地,为了更有利于入口气体中氧气浓度的调节,及扩大调节的范围,在燃料电池电堆与分子筛之间设置空气补充路及增湿器,将所述增湿器设置在分子筛与电堆之间,所述空气补充路的进气口设置在空压机与中冷器之间的空气进气管路,所述空气补充路的出气口设置在分子筛与增湿器之间的空气进气管路,通过空气补充路调节进入燃料电池电堆的氧气浓度。Preferably, in order to be more conducive to the adjustment of the oxygen concentration in the inlet gas and to expand the adjustment range, an air supplementary circuit and a humidifier are arranged between the fuel cell stack and the molecular sieve, and the humidifier is arranged between the molecular sieve and the electric sieve. Between the stacks, the air inlet of the air supplementary path is arranged in the air inlet line between the air compressor and the intercooler, and the air outlet of the air supplementary path is arranged in the air inlet between the molecular sieve and the humidifier. The gas pipeline is used to adjust the oxygen concentration entering the fuel cell stack through the air supplementary circuit.

优选地,可以通过空压机和其他设备降低分子筛的吸附压力,实现脱附分子筛吸附的氮气;脱附的氮气输入氮气脱附管路,在燃料电池工作模式将氮气通过氮气脱附管路的氮气尾排支路输入氢气尾排管路排出;在燃料电池吹扫模式将氮气通过氮气脱附管路的氮气吹扫支路输入燃料电池电堆的阴极室入口。Preferably, the adsorption pressure of the molecular sieve can be reduced by an air compressor and other equipment to realize the desorption of nitrogen adsorbed by the molecular sieve; the desorbed nitrogen is input into the nitrogen desorption pipeline, and the nitrogen is passed through the nitrogen desorption pipeline in the working mode of the fuel cell. The nitrogen tail exhaust branch is input into the hydrogen tail exhaust pipe and discharged; in the fuel cell purging mode, nitrogen is input into the cathode chamber inlet of the fuel cell stack through the nitrogen purging branch of the nitrogen desorption pipeline.

优选地,如图6所示,提供一种利用分子筛的氧气循环低尾排燃料电池空气控制方法,包括:Preferably, as shown in FIG. 6 , a method for controlling the air of an oxygen circulation low tail exhaust fuel cell using molecular sieves is provided, including:

S301启动燃料电池电堆,开启氧气循环燃料电池空气处理系统中氮气排出支路的阀门;S301 starts the fuel cell stack, and opens the valve of the nitrogen discharge branch in the oxygen cycle fuel cell air treatment system;

S302根据燃料电池电堆性能确定入堆的氧气浓度目标需求;S302 determines the target requirement of oxygen concentration into the stack according to the performance of the fuel cell stack;

S303通过控制阀门开度分配空气进气管路进入中冷器与空气补充路的空气流量;S303 distributes the air flow of the air intake pipe into the intercooler and the air supplementary circuit by controlling the valve opening;

S304将脱附后的氮气通过氢气尾排管路排出;S304 discharges the desorbed nitrogen gas through the hydrogen tailpipe;

S305按照预设条件控制第一分子筛及第二分子筛与空压机交替连通;S305 controls the first molecular sieve and the second molecular sieve to communicate alternately with the air compressor according to preset conditions;

S306控制开启氧气循环管路中的阀门,将电堆排出的氧气输入空气进气管路;S306 controls to open the valve in the oxygen circulation pipeline, and input the oxygen discharged from the stack into the air intake pipeline;

S307判断是否到达吹扫时机,若是,则转至S308;若否,则转至S305;S307 judges whether the purging timing is reached, if so, go to S308; if not, go to S305;

S308关闭氧气循环燃料电池空气处理系统中氮气排出支路的阀门;S308 closes the valve of the nitrogen discharge branch in the oxygen cycle fuel cell air treatment system;

S309降低空压机转速,减小空压机下游的阀门的开度;S309 reduces the speed of the air compressor and reduces the opening of the valve downstream of the air compressor;

S310确定吹扫结束,关机。S310 determines that the purging is over, and shuts down.

本实施例中,在S306中,除提高氧气浓度外,还设计了氧气循环管路,能够更有效的利用电堆的氧气湿度为入电堆气体增湿。也可以结合增湿器控制入堆气体湿度,更有利于调节及降低成本。In this embodiment, in S306, in addition to increasing the oxygen concentration, an oxygen circulation pipeline is also designed, which can more effectively utilize the oxygen humidity of the stack to humidify the gas entering the stack. It can also be combined with a humidifier to control the humidity of the incoming gas, which is more conducive to adjustment and cost reduction.

基于同一发明构思,本实施例还提供了一种燃料电池系统、车辆,由于该燃料电池系统、车辆所解决问题的原理与前述实施例的一种利用分子筛的氧气循环燃料电池空气处理系统相似,因此本实施例的实施可以参见前述一种利用分子筛的氧气循环燃料电池空气处理系统的实施,重复之处不再赘述。Based on the same inventive concept, this embodiment also provides a fuel cell system and a vehicle. Since the principle of the problem solved by the fuel cell system and the vehicle is similar to the oxygen cycle fuel cell air treatment system using molecular sieves in the foregoing embodiment, Therefore, for the implementation of this embodiment, reference may be made to the implementation of the aforementioned oxygen cycle fuel cell air treatment system using molecular sieves, and repeated details will not be repeated.

本发明实施例还提供了一种燃料电池系统,包括燃料电池电堆,所述燃料电池电堆的阴极室入口与上述任意一实施例所述的利用分子筛的氧气循环燃料电池空气处理系统的空气进气管路相连通。本实施例的燃料电池系统能够调节氧气的浓度,具有较高的效率和可靠性,且能够保证入堆氧气的湿度。An embodiment of the present invention further provides a fuel cell system, including a fuel cell stack, the inlet of the cathode chamber of the fuel cell stack is connected to the air of the oxygen cycle fuel cell air treatment system using molecular sieve described in any one of the above embodiments The intake pipes are connected. The fuel cell system of this embodiment can adjust the concentration of oxygen, has high efficiency and reliability, and can ensure the humidity of the oxygen entering the stack.

本发明实施例还提供了一种车辆,所述车辆包括如上任意实施例所述的燃料电池系统。Embodiments of the present invention also provide a vehicle, the vehicle including the fuel cell system described in any of the above embodiments.

在上述实施例中,可以按照氧气浓度需求匹配对应的分子筛的量或其他参数,从而实现按照需求提高电堆性能,可以利用空气补充路调节入堆氧气浓度,及实现氮气吹扫,降低尾排氢浓度,实施3中还能够实现氧气的循环,更方便地调节入堆气体的湿度。In the above embodiment, the corresponding molecular sieve amount or other parameters can be matched according to the oxygen concentration requirements, so as to improve the stack performance according to the requirements, the air supplementary circuit can be used to adjust the oxygen concentration in the stack, and nitrogen purging can be realized to reduce the tail exhaust. The hydrogen concentration, in implementation 3, can also realize the circulation of oxygen, and it is more convenient to adjust the humidity of the incoming gas.

说明书与权利要求中所使用的序数例如“第一”、“第二”等的用词,以修饰相应的元件,其本身并不意味着该元件有任何的序数,也不代表某一元件与另一元件的顺序,该些序数的使用仅用来使具有某命名的一元件得以和另一具有相同命名的元件能做出清楚区分。Words such as "first", "second", etc. used in the description and the claims are used to modify the corresponding element, which does not mean that the element has any ordinal number, nor does it mean that a certain element is related to the corresponding element. The order of another element, the use of the ordinal numbers is only used to clearly distinguish one element with a certain designation from another element with the same designation.

类似地,应当理解,为了精简本发明并帮助理解各个发明方面中的一个或多个,在上面对本发明的示例性实施例的描述中,本发明的各个特征有时被一起分组到单个实施例、图、或者对其的描述中。然而,并不应将该发明的方法解释成反映如下意图:即所要求保护的本发明要求比在每个权利要求中所明确记载的特征更多的特征。因此,遵循具体实施方式的权利要求书由此明确地并入该具体实施方式,其中每个权利要求本身都作为本发明的单独实施例。Similarly, it is to be understood that in the above description of exemplary embodiments of the invention, various features of the invention are sometimes grouped together into a single embodiment, figure, or its description. However, this method of the invention should not be construed to reflect the intention that the invention as claimed requires more features than are expressly recited in each claim. Thus, the claims following the Detailed Description are hereby expressly incorporated into this Detailed Description, with each claim standing on its own as a separate embodiment of this invention.

上面结合附图对本发明的实施例进行了描述,但是本发明并不局限于上述的具体实施方式,上述的具体实施方式仅仅是示意性的,而不是限制性的,本领域的普通技术人员在本发明的启示下,在不脱离本发明宗旨和权利要求所保护的范围情况下,还可做出很多形式,这些均属于本发明的保护之内。The embodiments of the present invention have been described above in conjunction with the accompanying drawings, but the present invention is not limited to the above-mentioned specific embodiments, which are merely illustrative rather than restrictive. Under the inspiration of the present invention, without departing from the scope of protection of the present invention and the claims, many forms can be made, which all belong to the protection of the present invention.

Claims (8)

1.一种利用分子筛的燃料电池空气控制方法,其特征在于,所述燃料电池空气控制方法包括,1. A fuel cell air control method utilizing molecular sieve is characterized in that, described fuel cell air control method comprises, 在空气进气管路中将分子筛设置在空压机的下游,并将所述分子筛设置在中冷器与燃料电池电堆之间,利用空压机增加分子筛的吸附压力,分子筛吸附空气中的氮气;The molecular sieve is arranged downstream of the air compressor in the air intake pipeline, and the molecular sieve is arranged between the intercooler and the fuel cell stack. The air compressor is used to increase the adsorption pressure of the molecular sieve, and the molecular sieve adsorbs nitrogen in the air. ; 空压机将分子筛吸附后的空气输入燃料电池电堆的阴极室入口;The air compressor feeds the air adsorbed by the molecular sieve into the inlet of the cathode chamber of the fuel cell stack; 降低分子筛的吸附压力,将分子筛吸附的氮气脱附,并通过氮气脱附管路排出至大气。Reduce the adsorption pressure of the molecular sieve, desorb the nitrogen adsorbed by the molecular sieve, and discharge it to the atmosphere through the nitrogen desorption pipeline. 2.如权利要求1所述的利用分子筛的燃料电池空气控制方法,其特征在于,所述燃料电池空气控制方法包括,2. The fuel cell air control method using molecular sieves according to claim 1, wherein the fuel cell air control method comprises: 至少设置第一分子筛与第二分子筛,将第一分子筛、第二分子筛分别与空压机、氮气脱附管路连接;At least a first molecular sieve and a second molecular sieve are arranged, and the first molecular sieve and the second molecular sieve are respectively connected to the air compressor and the nitrogen desorption pipeline; 当第一分子筛与空压机连通时,控制第二分子筛与氮气脱附管路连通;当第二分子筛与空压机连通时,控制第一分子筛与氮气脱附管路连通。When the first molecular sieve is communicated with the air compressor, the second molecular sieve is controlled to communicate with the nitrogen desorption pipeline; when the second molecular sieve is communicated with the air compressor, the first molecular sieve is controlled to communicate with the nitrogen desorption pipeline. 3.如权利要求1所述的利用分子筛的燃料电池空气控制方法,其特征在于,所述燃料电池空气控制方法包括,3. The fuel cell air control method using molecular sieves according to claim 1, wherein the fuel cell air control method comprises: 设置空气补充路,所述空气补充路的进气口设置在空压机与中冷器之间的空气进气管路,所述空气补充路的出气口设置在分子筛与燃料电池电堆之间的空气进气管路,通过空气补充路调节进入燃料电池电堆的氧气浓度。An air supplementary circuit is provided, the air inlet of the air supplementary circuit is arranged in the air intake pipeline between the air compressor and the intercooler, and the air outlet of the air supplementary circuit is arranged in the air inlet between the molecular sieve and the fuel cell stack. The air intake line adjusts the oxygen concentration entering the fuel cell stack through the air supplementary line. 4.如权利要求3所述的利用分子筛的燃料电池空气控制方法,其特征在于,所述燃料电池空气控制方法包括,4. The fuel cell air control method using molecular sieves according to claim 3, wherein the fuel cell air control method comprises: 根据燃料电池电堆性能确定入堆的氧气浓度目标需求;Determine the target requirement of oxygen concentration into the stack according to the performance of the fuel cell stack; 通过控制空气补充路阀门的开度分配空气进气管路与空气补充路的空气流量。By controlling the opening of the air supplementary circuit valve, the air flow of the air intake line and the air supplementary circuit is distributed. 5.如权利要求2所述的利用分子筛的燃料电池空气控制方法,其特征在于,所述燃料电池空气控制方法包括,按照预设条件控制第一分子筛及第二分子筛与空压机交替连通。5 . The fuel cell air control method using molecular sieves according to claim 2 , wherein the fuel cell air control method comprises: controlling the first molecular sieve and the second molecular sieve to communicate alternately with the air compressor according to preset conditions. 6 . 6.如权利要求5所述的利用分子筛的燃料电池空气控制方法,其特征在于,所述燃料电池空气控制方法包括,6. The fuel cell air control method using molecular sieves according to claim 5, wherein the fuel cell air control method comprises: 所述预设条件为根据燃料电池工况及分子筛的性能确定的交替设定时间,当达到交替设定时间时,切换第一分子筛、第二分子筛与空压机之间的阀门。The preset condition is an alternate setting time determined according to the working conditions of the fuel cell and the performance of the molecular sieve. When the alternate setting time is reached, the valves between the first molecular sieve, the second molecular sieve and the air compressor are switched. 7.如权利要求1所述的利用分子筛的燃料电池空气控制方法,其特征在于,所述燃料电池空气控制方法包括,7. The fuel cell air control method using molecular sieves according to claim 1, wherein the fuel cell air control method comprises: 通过断开分子筛与空压机的连通降低分子筛的吸附压力,使分子筛脱附氮气;Reduce the adsorption pressure of the molecular sieve by disconnecting the connection between the molecular sieve and the air compressor, so that the molecular sieve can desorb nitrogen; 在燃料电池工作模式下,将氮气通过氮气脱附管路的氮气排出支路排出至大气;In the working mode of the fuel cell, the nitrogen is discharged to the atmosphere through the nitrogen discharge branch of the nitrogen desorption pipeline; 在燃料电池吹扫模式下,将氮气通过氮气脱附管路的氮气吹扫支路输入燃料电池电堆的阴极室入口。In the fuel cell purge mode, nitrogen is fed into the cathode chamber inlet of the fuel cell stack through the nitrogen purge branch of the nitrogen desorption pipeline. 8.如权利要求7所述的利用分子筛的燃料电池空气控制方法,其特征在于,所述燃料电池空气控制方法还包括,8. The fuel cell air control method using molecular sieves according to claim 7, wherein the fuel cell air control method further comprises: 根据燃料电池系统的关机状态确定吹扫时机;Determine the purging timing according to the shutdown state of the fuel cell system; 当判定到达吹扫时机时,启动燃料电池吹扫模式,关闭氮气排出支路的阀门;When it is determined that the purging timing is reached, the fuel cell purging mode is activated, and the valve of the nitrogen discharge branch is closed; 降低空压机转速,减小空压机下游的阀门的开度。Reduce the speed of the air compressor and reduce the opening of the valve downstream of the air compressor.
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