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CN110444785A - Dual polar plates of proton exchange membrane fuel cell, battery and battery pile - Google Patents

Dual polar plates of proton exchange membrane fuel cell, battery and battery pile Download PDF

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Publication number
CN110444785A
CN110444785A CN201910815685.8A CN201910815685A CN110444785A CN 110444785 A CN110444785 A CN 110444785A CN 201910815685 A CN201910815685 A CN 201910815685A CN 110444785 A CN110444785 A CN 110444785A
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China
Prior art keywords
plate
proton exchange
exchange membrane
fuel cell
membrane fuel
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Chinese (zh)
Inventor
刘贵生
万忠民
孔祥忠
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Hunan Technological Fuel Cell Co Ltd
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Hunan Technological Fuel Cell Co Ltd
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Priority to CN201910815685.8A priority Critical patent/CN110444785A/en
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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
    • H01M8/02Details
    • H01M8/0202Collectors; Separators, e.g. bipolar separators; Interconnectors
    • H01M8/023Porous and characterised by the material
    • H01M8/0232Metals or alloys
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/02Details
    • H01M8/0202Collectors; Separators, e.g. bipolar separators; Interconnectors
    • H01M8/0258Collectors; Separators, e.g. bipolar separators; Interconnectors characterised by the configuration of channels, e.g. by the flow field of the reactant or coolant
    • H01M8/026Collectors; Separators, e.g. bipolar separators; Interconnectors characterised by the configuration of channels, e.g. by the flow field of the reactant or coolant characterised by grooves, e.g. their pitch or depth
    • 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
    • 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
    • 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
    • H01M8/04201Reactant storage and supply, e.g. means for feeding, pipes
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/24Grouping of fuel cells, e.g. stacking of fuel cells
    • H01M8/2457Grouping of fuel cells, e.g. stacking of fuel cells with both reactants being gaseous or vaporised
    • 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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  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Sustainable Development (AREA)
  • Sustainable Energy (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Fuel Cell (AREA)

Abstract

本发明涉及燃料电池技术领域,尤其是涉及一种质子交换膜燃料电池双极板、电池及电池堆;包括紧压于一体的阳极板和阴极板;阳极板和阴极板的板面上均开设有凹槽;阳极板和阴极板上均开设有燃料气体入口、燃料气体出口、氧化剂气体入口、氧化剂气体出口及排水口;其中,阳极板上的燃料气体入口和燃料气体出口均与阳极板上的凹槽连通;阴极板上的氧化剂气体入口和氧化剂气体出口均与阴极板上的凹槽连通,各凹槽内填充有多孔三维基底填充块;通过质子交换膜燃料电池双极板的结构设计以解决现有双极板较薄,在双极板上开设凹槽,并在凹槽内设置气体流道,加工工艺复杂,同时不利于气体的扩散,同时流道的设计,不利于水的及时排出技术问题。

The invention relates to the technical field of fuel cells, in particular to a proton exchange membrane fuel cell bipolar plate, a battery and a battery stack; it includes an anode plate and a cathode plate tightly pressed together; There are grooves; the anode plate and the cathode plate are provided with a fuel gas inlet, a fuel gas outlet, an oxidant gas inlet, an oxidant gas outlet and a drain; wherein, the fuel gas inlet and the fuel gas outlet on the anode plate are connected to the anode plate The grooves of the cathode plate are connected; the oxidant gas inlet and the oxidant gas outlet on the cathode plate are connected with the grooves on the cathode plate, and each groove is filled with a porous three-dimensional substrate filling block; through the structural design of the proton exchange membrane fuel cell bipolar plate To solve the problem that the existing bipolar plate is thin, grooves are set on the bipolar plate, and gas flow channels are set in the grooves. The processing technology is complicated, and it is not conducive to the diffusion of gas. Troubleshoot technical issues in a timely manner.

Description

质子交换膜燃料电池双极板、电池及电池堆Proton exchange membrane fuel cell bipolar plates, cells and cell stacks

技术领域technical field

本发明涉及燃料电池技术领域,尤其是涉及一种质子交换膜燃料电池双极板、电池及电池堆。The invention relates to the technical field of fuel cells, in particular to a proton exchange membrane fuel cell bipolar plate, a battery and a battery stack.

背景技术Background technique

燃料电池是一种将氢和氧的化学能通过电极反应直接转化为电能的装置。燃料电池通常由多个电池单元构成,每个电池单元包括两个电极(阳极和阴极),两个电极被电解质元件隔开,并且彼此串联地组装,形成燃料电池堆。通过给每个电极供给适当的反应物,即给一个电极供给燃料而另一个供给氧化剂,实现电化学反应,从而在电极之间形成电位差,并且因此产生电能。A fuel cell is a device that converts the chemical energy of hydrogen and oxygen directly into electrical energy through an electrode reaction. A fuel cell is generally constructed of a plurality of cells, each cell comprising two electrodes (an anode and a cathode), separated by an electrolyte element, and assembled in series with each other to form a fuel cell stack. The electrochemical reaction is achieved by supplying the appropriate reactants to each electrode, ie fuel to one electrode and oxidant to the other, creating a potential difference between the electrodes and thereby generating electrical energy.

双极板上一般设有三进三出孔,六个孔均通过进、出流体通道与中间反应区域的气体流道连通,气体进入电池堆后由进、出流体流道阴导进入流体在MEA表面发生反应。现有的双极板均开设有气体流道,然而,为了减少对电流和热的传导阻力,双极板的较薄,在双极板上开设凹槽,并在凹槽内设置气体流道,加工工艺复杂,同时不利于气体的扩散,降低反应速率,同时流道的设计,不利于水的及时排出。There are generally three inlets and three outlets on the bipolar plate, and the six holes are connected with the gas flow channel in the middle reaction area through the inlet and outlet fluid channels. The surface reacts. Existing bipolar plates are provided with gas channels. However, in order to reduce the resistance to current and heat conduction, the bipolar plates are thinner, and grooves are opened on the bipolar plates, and gas channels are arranged in the grooves. , the processing technology is complicated, and it is not conducive to the diffusion of gas and reduces the reaction rate. At the same time, the design of the flow channel is not conducive to the timely discharge of water.

因此,针对上述问题本发明急需提供一种质子交换膜燃料电池双极板、电池及电池堆。Therefore, in view of the above problems, the present invention urgently needs to provide a proton exchange membrane fuel cell bipolar plate, battery and battery stack.

发明内容Contents of the invention

本发明的目的在于提供一种质子交换膜燃料电池双极板、电池及电池堆,通过质子交换膜燃料电池双极板的结构设计以解决现有技术中存在的双极板较薄,在双极板上开设凹槽,并在凹槽内设置气体流道,加工工艺复杂,同时不利于气体的扩散,降低反应速率,同时流道的设计,不利于水的及时排出的技术问题。The purpose of the present invention is to provide a proton exchange membrane fuel cell bipolar plate, battery and cell stack, through the structural design of the proton exchange membrane fuel cell bipolar plate to solve the thin bipolar plate existing in the prior art Grooves are set on the electrode plate, and gas flow channels are set in the grooves. The processing technology is complicated, and it is not conducive to the diffusion of gas and reduces the reaction rate. At the same time, the design of the flow channels is not conducive to the technical problem of timely discharge of water.

本发明提供的一种质子交换膜燃料电池双极板,包括紧压于一体的阳极板和阴极板;阳极板和阴极板的板面上均开设有凹槽;阳极板和阴极板上均开设有燃料气体入口、燃料气体出口、氧化剂气体入口、氧化剂气体出口及排水口;其中,阳极板上的燃料气体入口和燃料气体出口均与阳极板上的凹槽连通;阴极板上的氧化剂气体入口和氧化剂气体出口均与阴极板上的凹槽连通,各凹槽内填充有多孔三维基底填充块。A proton exchange membrane fuel cell bipolar plate provided by the invention comprises an anode plate and a cathode plate tightly pressed together; grooves are opened on the surface of the anode plate and the cathode plate; grooves are opened on the anode plate and the cathode plate There are fuel gas inlets, fuel gas outlets, oxidant gas inlets, oxidant gas outlets and drains; wherein, the fuel gas inlets and fuel gas outlets on the anode plate are connected to the grooves on the anode plate; the oxidant gas inlets on the cathode plate Both the gas outlet and the oxidant gas outlet communicate with the grooves on the cathode plate, and each groove is filled with porous three-dimensional base filling blocks.

优选地,凹槽的内底部呈平面设置。Preferably, the inner bottom of the groove is arranged on a plane.

优选地,凹槽的深度为0.05mm-1mm。Preferably, the depth of the groove is 0.05mm-1mm.

优选地,多孔三维基底填充块为多孔镍网。Preferably, the porous three-dimensional base packing block is a porous nickel mesh.

优选地,多孔三维基底填充块的孔隙率为85%-98%。Preferably, the porosity of the porous three-dimensional base packing block is 85%-98%.

优选地,多孔三维基底填充块的厚度为0.05mm-1mm。Preferably, the thickness of the porous three-dimensional base packing block is 0.05mm-1mm.

优选地,阳极板的外板面和内板面上均设有凹槽,阴极板的外板面设有凹槽。Preferably, grooves are provided on the outer surface and inner surface of the anode plate, and grooves are provided on the outer surface of the cathode plate.

本发明还包括一种质子交换膜燃料电池,包括多个并排设置的如上述中任一项所述的质子交换膜燃料电池双极板相邻两质子交换膜燃料电池双极板间设有质子交换膜。The present invention also includes a proton exchange membrane fuel cell, comprising a plurality of proton exchange membrane fuel cell bipolar plates arranged side by side as described in any one of the above proton exchange membrane fuel cell bipolar plates are provided with protons between adjacent two proton exchange membrane fuel cell bipolar plates exchange membrane.

本发明还包括一种电池堆,包括两相对设置的左端板和右端板,左端板和右端板间设有多个叠放的如上述所述的质子交换膜燃料电池。The present invention also includes a cell stack, which includes two oppositely arranged left end plates and right end plates, and a plurality of stacked proton exchange membrane fuel cells as described above are arranged between the left end plates and the right end plates.

优选地,左端板从上到下依次设有与左端板贯通的氧化剂气体输入口、水输入口和燃料气体输入口,右端板上设有与右端板贯通的燃料气体输出口,水输出口和氧化剂气体输出口。Preferably, the left end plate is sequentially provided with an oxidant gas input port, a water input port and a fuel gas input port connected with the left end plate from top to bottom, and the right end plate is provided with a fuel gas output port connected with the right end plate, a water output port and a Oxidant gas outlet.

本发明提供的一种质子交换膜燃料电池双极板、电池及电池堆与现有技术相比具有以下进步:A kind of proton exchange membrane fuel cell bipolar plate, battery and battery stack provided by the present invention have following progress compared with prior art:

1、本发明通过紧压于一体的阳极板和阴极板;阳极板和阴极板的板面上均开设有凹槽;阳极板和阴极板上均开设有燃料气体入口、燃料气体出口、氧化剂气体入口、氧化剂气体出口及排水口;其中,阳极板上的燃料气体入口和燃料气体出口均与阳极板上的凹槽连通;阴极板上的氧化剂气体入口和氧化剂气体出口均与阴极板上的凹槽连通,各凹槽内填充有多孔三维基底填充块;多孔三维基底填充块为多孔镍网;凹槽的内底部呈平面设置的设计,采用高孔隙率的多孔三维基底填充块填充凹槽,凹槽内不再设置气体流道,只填充有多孔三维基底填充块,同时保证凹槽的内底部呈平面设置,使得多孔三维基底填充块与凹槽地面紧密贴合,当燃料气体和氧化剂气体分别从阳极板和阴极板进入对应的凹槽内,燃料气体和氧化剂气体分别在对应多孔三维基底填充块内扩散,保证燃料气体和氧化剂气体的扩散的均匀性,从而保证燃料气体和氧化剂气体发生反应的稳定性;排水口的设计有利于反应过程中生产水的排出;由多孔镍网填充的凹槽即可以实现三维流道的架构,可以免去在阳极板和阴极板开设流道,降低了加工的难度和成本。1. In the present invention, the anode plate and the cathode plate are tightly pressed together; the anode plate and the cathode plate are provided with grooves; the anode plate and the cathode plate are provided with a fuel gas inlet, a fuel gas outlet, and an oxidant gas Inlet, oxidant gas outlet and drain; wherein, the fuel gas inlet and fuel gas outlet on the anode plate are connected to the groove on the anode plate; the oxidant gas inlet and oxidant gas outlet on the cathode plate are connected to the groove on the cathode plate The grooves are connected, and each groove is filled with a porous three-dimensional base filling block; the porous three-dimensional base filling block is a porous nickel mesh; the inner bottom of the groove is designed as a plane, and the porous three-dimensional base filling block with high porosity is used to fill the groove. The groove is no longer provided with a gas flow channel, and only filled with porous three-dimensional base filling blocks, while ensuring that the inner bottom of the groove is set on a plane, so that the porous three-dimensional base filling blocks are closely attached to the ground of the groove. When the fuel gas and oxidant gas Enter the corresponding grooves from the anode plate and the cathode plate respectively, and the fuel gas and oxidant gas diffuse in the corresponding porous three-dimensional substrate filling blocks to ensure the uniformity of the diffusion of the fuel gas and oxidant gas, thereby ensuring the generation of fuel gas and oxidant gas. The stability of the reaction; the design of the drain port is conducive to the discharge of production water during the reaction process; the groove filled with porous nickel mesh can realize the structure of the three-dimensional flow channel, which can eliminate the need to open flow channels on the anode plate and the cathode plate, reducing the The difficulty and cost of processing.

2、本发明中的凹槽的深度为0.05mm-1mm;本实施例优选的凹槽的深度为1mm;多孔三维基底填充块的厚度为0.05mm-1mm;本实施例优选的多孔三维基底填充块的厚度为1mm,方便加工,安装方便,同时保证对气体的有效扩散。2. The depth of the groove in the present invention is 0.05mm-1mm; the depth of the preferred groove in this embodiment is 1mm; the thickness of the porous three-dimensional substrate filling block is 0.05mm-1mm; the preferred porous three-dimensional substrate filling in this embodiment The thickness of the block is 1mm, which is convenient for processing and installation, and at the same time ensures the effective diffusion of gas.

3、本发明中多孔三维基底填充块的孔隙率为85%-98%;保证孔的密实度,保证对气体的有效扩散。3. The porosity of the porous three-dimensional base filling block in the present invention is 85%-98%, which ensures the compactness of the pores and the effective diffusion of gas.

4、本发明通过阳极板的外板面和内板面上均设有凹槽,阴极板的外板面设有凹槽的设计,进一步保证燃料气体扩散的均匀性,保证燃料气体与氧化剂气体反应的均匀性,从而保证电量的稳定供应,保证汽车行驶的安全性。4. The present invention is provided with grooves on the outer surface and inner surface of the anode plate, and the design of grooves on the outer surface of the cathode plate further ensures the uniformity of fuel gas diffusion and ensures that the fuel gas and oxidant gas The uniformity of the reaction ensures the stable supply of electricity and the safety of the car.

附图说明Description of drawings

为了更清楚地说明本发明具体实施方式或现有技术中的技术方案,下面将对具体实施方式或现有技术描述中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图是本发明的一些实施方式,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据这些附图获得其他的附图。In order to more clearly illustrate the specific implementation of the present invention or the technical solutions in the prior art, the following will briefly introduce the accompanying drawings that need to be used in the specific implementation or description of the prior art. Obviously, the accompanying drawings in the following description The drawings show some implementations of the present invention, and those skilled in the art can obtain other drawings based on these drawings without any creative work.

图1为本发明中所述质子交换膜燃料电池双极板的结构示意图(主视剖视图);Fig. 1 is the structural representation (front sectional view) of proton exchange membrane fuel cell bipolar plate described in the present invention;

图2为本发明所述阳极板的结构示意图(立体图);Fig. 2 is the structural representation (perspective view) of anode plate of the present invention;

图3为本发明中所述电池的结构示意图(主视剖视图);Fig. 3 is a schematic structural view (front sectional view) of the battery described in the present invention;

图4为本发明中所述电池堆的结构示意图(主视剖视图)。Fig. 4 is a schematic structural view (front sectional view) of the battery stack in the present invention.

附图标记说明:Explanation of reference signs:

1、阳极板;2、阴极板;3、凹槽;4、燃料气体入口;5、燃料气体出口;6、氧化剂气体入口;7、氧化剂气体出口;9、多孔三维基底填充块;8、排水口;10、质子交换膜;11、氧化剂气体输入口;12、水输入口;13、燃料气体输入口;14、左端板;15、右端板;16、燃料气体输出口;17、水输出口;18、氧化剂气体输出口;1. Anode plate; 2. Cathode plate; 3. Groove; 4. Fuel gas inlet; 5. Fuel gas outlet; 6. Oxidant gas inlet; 7. Oxidant gas outlet; 9. Porous three-dimensional substrate filling block; 8. Drainage 10, proton exchange membrane; 11, oxidant gas input port; 12, water input port; 13, fuel gas input port; 14, left end plate; 15, right end plate; 16, fuel gas output port; 17, water output port ; 18. Oxidant gas outlet;

具体实施方式Detailed ways

下面将结合附图对本发明的技术方案进行清楚、完整地描述,显然,所描述的实施例是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。The technical solutions of the present invention will be clearly and completely described below in conjunction with the accompanying drawings. Apparently, the described embodiments are some of the embodiments of the present invention, but not all of them. Based on the embodiments of the present invention, all other embodiments obtained by persons of ordinary skill in the art without making creative efforts belong to the protection scope of the present invention.

在本发明的描述中,需要说明的是,术语“中心”、“上”、“下”、“左”、“右”、“竖直”、“水平”、“内”、“外”等指示的方位或位置关系为基于附图所示的方位或位置关系,仅是为了便于描述本发明和简化描述,而不是指示或暗示所指的装置或元件必须具有特定的方位、以特定的方位构造和操作,因此不能理解为对本发明的限制。此外,术语“第一”、“第二”、“第三”仅用于描述目的,而不能理解为指示或暗示相对重要性。In the description of the present invention, it should be noted that the terms "center", "upper", "lower", "left", "right", "vertical", "horizontal", "inner", "outer" etc. The indicated orientation or positional relationship is based on the orientation or positional relationship shown in the drawings, and is only for the convenience of describing the present invention and simplifying the description, rather than indicating or implying that the referred device or element must have a specific orientation, or in a specific orientation. construction and operation, therefore, should not be construed as limiting the invention. In addition, the terms "first", "second", and "third" are used for descriptive purposes only, and should not be construed as indicating or implying relative importance.

在本发明的描述中,需要说明的是,除非另有明确的规定和限定,术语“安装”、“相连”、“连接”应做广义理解,例如,可以是固定连接,也可以是可拆卸连接,或一体地连接;可以是机械连接,也可以是电连接;可以是直接相连,也可以通过中间媒介间接相连,可以是两个元件内部的连通。对于本领域的普通技术人员而言,可以具体情况理解上述术语在本发明中的具体含义。In the description of the present invention, it should be noted that unless otherwise specified and limited, the terms "installation", "connection" and "connection" should be understood in a broad sense, for example, it can be a fixed connection or a detachable connection. Connected, or integrally connected; it can be mechanically connected or electrically connected; it can be directly connected or indirectly connected through an intermediary, and it can be the internal communication of two components. Those of ordinary skill in the art can understand the specific meanings of the above terms in the present invention in specific situations.

如图1所示,本实施例中提供的一种质子交换膜燃料电池双极板,包括紧压于一体的阳极板1和阴极板2;阳极板1和阴极板2的板面上均开设有凹槽3;阳极板1和阴极板2上均开设有燃料气体入口4、燃料气体出口5、氧化剂气体入口6、氧化剂气体出口7及排水口8;其中,阳极板1上的燃料气体入口4和燃料气体出口5均与阳极板1上的凹槽3连通;阴极板2上的氧化剂气体入口6和氧化剂气体出口7均与阴极板2上的凹槽3连通,各凹槽3内填充有多孔三维基底填充块9;多孔三维基底填充块为多孔镍网;凹槽2的内底部呈平面设置。As shown in Figure 1, a kind of proton exchange membrane fuel cell bipolar plate provided in the present embodiment comprises anode plate 1 and cathode plate 2 tightly pressed together; There are grooves 3; the anode plate 1 and the cathode plate 2 are provided with a fuel gas inlet 4, a fuel gas outlet 5, an oxidant gas inlet 6, an oxidant gas outlet 7 and a water outlet 8; wherein, the fuel gas inlet on the anode plate 1 4 and the fuel gas outlet 5 are all communicated with the groove 3 on the anode plate 1; the oxidant gas inlet 6 and the oxidant gas outlet 7 on the cathode plate 2 are all communicated with the groove 3 on the cathode plate 2, and each groove 3 is filled with There is a porous three-dimensional base filling block 9; the porous three-dimensional base filling block is a porous nickel mesh; the inner bottom of the groove 2 is arranged on a plane.

本发明通过紧压于一体的阳极板1和阴极板2;阳极板1和阴极板2的板面上均开设有凹槽3;阳极板1和阴极板2上均开设有燃料气体入口4、燃料气体出口5、氧化剂气体入口6、氧化剂气体出口7及排水口8;其中,阳极板1上的燃料气体入口4和燃料气体出口5均与阳极板1上的凹槽3连通;阴极板2上的氧化剂气体入口6和氧化剂气体出口7均与阴极板2上的凹槽3连通,各凹槽3内填充有多孔三维基底填充块9;多孔三维基底填充块为多孔镍网;凹槽3的内底部呈平面设置的设计,采用高孔隙率的多孔三维基底填充块9填充凹槽3,凹槽3内不再设置气体流道,只填充有多孔三维基底填充块,同时保证凹槽2的内底部呈平面设置,使得多孔三维基底填充块与凹槽3地面紧密贴合,当燃料气体和氧化剂气体分别从阳极板1和阴极板2进入对应的凹槽3内,燃料气体和氧化剂气体分别在对应多孔三维基底填充块9内扩散,保证燃料气体和氧化剂气体的扩散的均匀性,从而保证燃料气体和氧化剂气体发生反应的稳定性;排水口8的设计有利于反应过程中生产水的排出;由多孔镍网填充的凹槽3即可以实现三维流道的架构,可以免去在阳极板和阴极板开设流道,降低了加工的难度和成本。In the present invention, the anode plate 1 and the cathode plate 2 are tightly pressed together; the anode plate 1 and the cathode plate 2 are provided with grooves 3; the anode plate 1 and the cathode plate 2 are provided with fuel gas inlets 4, Fuel gas outlet 5, oxidant gas inlet 6, oxidant gas outlet 7 and drain port 8; wherein, the fuel gas inlet 4 and fuel gas outlet 5 on the anode plate 1 are all communicated with the groove 3 on the anode plate 1; the cathode plate 2 The oxidant gas inlet 6 and the oxidant gas outlet 7 on the cathode plate 2 are all in communication with the groove 3 on the cathode plate 2, and each groove 3 is filled with a porous three-dimensional base filling block 9; the porous three-dimensional base filling block is a porous nickel mesh; the groove 3 The inner bottom of the tank is designed with a plane setting, and the groove 3 is filled with a porous three-dimensional base filling block 9 with high porosity. The gas flow channel is no longer arranged in the groove 3, and only the porous three-dimensional base filling block is filled, while ensuring that the groove 2 The inner bottom of the tank is set in a plane, so that the porous three-dimensional base filling block is closely attached to the ground of the groove 3. When the fuel gas and the oxidant gas enter the corresponding groove 3 from the anode plate 1 and the cathode plate 2 respectively, the fuel gas and the oxidant gas Diffusion in the corresponding porous three-dimensional base packing block 9 respectively, to ensure the uniformity of the diffusion of the fuel gas and the oxidant gas, thereby ensuring the stability of the reaction between the fuel gas and the oxidant gas; the design of the outlet 8 is conducive to the production of water during the reaction process Discharge; the groove 3 filled with porous nickel mesh can realize the structure of the three-dimensional flow channel, which can save the opening of the flow channel on the anode plate and the cathode plate, and reduce the difficulty and cost of processing.

本发明重点在于在凹槽3内填充多孔三维基底填充块9,使得凹槽3内构成三维流场结构,保证气体的稳定扩散,扩散的更加均匀,保证进入反应区的流畅性,无需在凹槽3内部开设流道,流道加工复杂,影响阴极板或者阳极板的刚性,由此本发明在凹槽3内填充多孔三维基底填充块9设计,大大降低了阳极板和阴极板的生产难度,同时保证反应的稳定进行,保证为汽车提供稳定的动力;多孔三维基底填充块9周壁与凹槽3内壁紧密贴合,保证三维流场结构的设计的精准性。The key point of the present invention is to fill the porous three-dimensional base filling block 9 in the groove 3, so that the three-dimensional flow field structure is formed in the groove 3 to ensure the stable diffusion of the gas, the diffusion is more uniform, and the smoothness of entering the reaction zone is ensured. A flow channel is set inside the groove 3, and the processing of the flow channel is complicated, which affects the rigidity of the cathode plate or the anode plate. Therefore, the present invention fills the groove 3 with a porous three-dimensional base filling block 9 design, which greatly reduces the production difficulty of the anode plate and the cathode plate. , and at the same time ensure the stable progress of the reaction and provide stable power for the car; the 9 peripheral walls of the porous three-dimensional base filling block and the inner wall of the groove 3 are closely attached to ensure the accuracy of the design of the three-dimensional flow field structure.

本发明中的凹槽3的深度为0.05mm-1mm;本实施例优选的凹槽3的深度为1mm;多孔三维基底填充块9的厚度为0.05mm-1mm;本实施例优选的多孔三维基底填充块9的厚度为1mm,方便加工,安装方便,同时保证对气体的有效扩散。The depth of the groove 3 in the present invention is 0.05mm-1mm; the depth of the preferred groove 3 of the present embodiment is 1mm; the thickness of the porous three-dimensional substrate filling block 9 is 0.05mm-1mm; the preferred porous three-dimensional substrate of the present embodiment The thickness of the filling block 9 is 1 mm, which is convenient for processing and installation, and at the same time ensures effective diffusion of gas.

本发明中多孔三维基底填充块9的孔隙率为85%-98%;保证孔的密实度,保证对气体的有效扩散。In the present invention, the porosity of the porous three-dimensional base packing block 9 is 85%-98%, which ensures the compactness of the pores and the effective diffusion of gas.

如图1所示,本实施例中的阳极板1的外板面和内板面上均设有凹槽3,阴极板2的外板面设有凹槽3。As shown in FIG. 1 , grooves 3 are provided on the outer and inner surfaces of the anode plate 1 in this embodiment, and grooves 3 are provided on the outer surface of the cathode plate 2 .

本发明通过阳极板1的外板面和内板面上均设有凹槽3,阴极板2的外板面设有凹槽3的设计,进一步保证燃料气体扩散的均匀性,保证燃料气体与氧化剂气体反应的均匀性,从而保证电量的稳定供应,保证汽车行驶的安全性。In the present invention, grooves 3 are provided on the outer surface and the inner surface of the anode plate 1, and the outer surface of the cathode plate 2 is provided with the design of the groove 3, which further ensures the uniformity of fuel gas diffusion and ensures that the fuel gas and The uniformity of the oxidant gas reaction ensures the stable supply of electricity and the safety of the car.

本发明还包括一种质子交换膜燃料电池,包括多个并排设置的如上述中任一项所述的质子交换膜燃料电池双极板相邻两质子交换膜燃料电池双极板间设有质子交换膜10。The present invention also includes a proton exchange membrane fuel cell, comprising a plurality of proton exchange membrane fuel cell bipolar plates arranged side by side as described in any one of the above proton exchange membrane fuel cell bipolar plates are provided with protons between adjacent two proton exchange membrane fuel cell bipolar plates exchange membrane 10.

如图4所示,本发明还包括一种电池堆,包括两相对设置的左端板14和右端板15,左端板14和右端板15间设有多个叠放的如上述所述的质子交换膜燃料电池;左端板14从上到下依次设有与左端板14贯通的氧化剂气体输入口11、水输入口12和燃料气体输入口13,右端板15上设有与右端板15贯通的燃料气体输出口16,水输出口17和氧化剂气体输出口18。As shown in Figure 4, the present invention also includes a battery stack, including two oppositely arranged left end plates 14 and right end plates 15, between the left end plate 14 and the right end plate 15 are provided with a plurality of stacked proton exchange devices as described above Membrane fuel cell; the left end plate 14 is sequentially provided with an oxidant gas input port 11, a water input port 12, and a fuel gas input port 13 that are connected with the left end plate 14 from top to bottom, and the right end plate 15 is provided with a fuel gas that is connected with the right end plate 15. Gas outlet 16, water outlet 17 and oxidant gas outlet 18.

质子交换膜燃料电池双极板的制备过程为:The preparation process of the bipolar plate of the proton exchange membrane fuel cell is as follows:

在阳极板1的外板面和内侧板面上均开设凹槽3,在阴极板2的外板面上开设凹槽3,将阳极板1的外板面上的凹槽、阳极板1的内板面上的凹槽和阴极板2的外板面上的凹槽内均填充多孔三维基底填充块9,将填充有多孔三维基底填充块9的阳极板1的内板面和阴极板2内板面紧贴组成双极板。All offer groove 3 on the outer plate surface of anode plate 1 and the inner plate surface, offer groove 3 on the outer plate surface of cathode plate 2, the groove on the outer plate surface of positive plate 1, the groove of anode plate 1 The grooves on the inner plate surface and the grooves on the outer plate surface of the cathode plate 2 are all filled with porous three-dimensional base filling blocks 9, and the inner plate surface of the anode plate 1 and the cathode plate 2 filled with the porous three-dimensional base filling blocks 9 The inner plate is closely attached to form a bipolar plate.

质子交换膜燃料电池的制备过程为:将两个质子交换膜燃料电池双极板平行放置,在两质子交换膜燃料电池双极板放置质子交换膜10,夹紧组成质子交换膜燃料电池。The preparation process of the proton exchange membrane fuel cell is as follows: place two proton exchange membrane fuel cell bipolar plates in parallel, place a proton exchange membrane 10 on the two proton exchange membrane fuel cell bipolar plates, and clamp to form a proton exchange membrane fuel cell.

电池堆的制备过程为:将多个质子交换膜燃料电池叠放于一体,在两侧放置端板,夹紧组成电池堆。The preparation process of the cell stack is as follows: a plurality of proton exchange membrane fuel cells are stacked together, end plates are placed on both sides, and the cell stack is formed by clamping.

电池堆的工作过程:将氢气从左端板14的燃料气体输入口13输入,将氧气从左端板14上的氧化剂气体输出口11输入,氢气从阳极板1上的燃料气体入口4进入凹槽3,在多孔三维基底填充块9流动扩散,目的是实现氢气进入反应区后扩散的更加均匀,扩散后,氢气从燃料气体出口5进入到质子交换膜10;氧气从阴极板2上的氧化剂气体入口6进入凹槽,进入阴极板2凹槽3内的多孔三维基底填充块9,在多孔三维基底填充块9流动扩散,目的是实现氧气进入反应区后扩散的更加均匀,扩散后氧气从氧化剂气体出口7进入质子交换膜10与氢气反应,反应生产的水依次从排水口8和水输出口17排出。The working process of the battery stack: hydrogen is input from the fuel gas input port 13 on the left end plate 14, oxygen is input from the oxidant gas output port 11 on the left end plate 14, and hydrogen enters the groove 3 from the fuel gas inlet 4 on the anode plate 1 , flows and diffuses in the porous three-dimensional substrate packing block 9, the purpose is to achieve a more uniform diffusion of hydrogen gas after entering the reaction zone. After diffusion, hydrogen gas enters the proton exchange membrane 10 from the fuel gas outlet 5; oxygen gas enters from the oxidant gas inlet on the cathode plate 2 6 enters the groove, enters the porous three-dimensional base filling block 9 in the groove 3 of the cathode plate 2, and flows and diffuses in the porous three-dimensional base filling block 9. The purpose is to realize a more uniform diffusion of oxygen after entering the reaction zone. The outlet 7 enters the proton exchange membrane 10 to react with hydrogen, and the water produced by the reaction is discharged from the water outlet 8 and the water outlet 17 in sequence.

最后应说明的是:以上各实施例仅用以说明本发明的技术方案,而非对其限制;尽管参照前述各实施例对本发明进行了详细的说明,本领域的普通技术人员应当理解:其依然可以对前述各实施例所记载的技术方案进行修改,或者对其中部分或者全部技术特征进行等同替换;而这些修改或者替换,并不使相应技术方案的本质脱离本发明各实施例技术方案的范围。Finally, it should be noted that: the above embodiments are only used to illustrate the technical solutions of the present invention, rather than limiting them; although the present invention has been described in detail with reference to the foregoing embodiments, those of ordinary skill in the art should understand that: It is still possible to modify the technical solutions described in the foregoing embodiments, or perform equivalent replacements for some or all of the technical features; and these modifications or replacements do not make the essence of the corresponding technical solutions deviate from the technical solutions of the various embodiments of the present invention. scope.

Claims (10)

1. a kind of dual polar plates of proton exchange membrane fuel cell, it is characterised in that: including pressing in the anode plate (1) and cathode of one Plate (2);Fluted (3) are opened up in the plate face of anode plate (1) and cathode plate (2);It is opened on anode plate (1) and cathode plate (2) Equipped with fuel gas inlet (4), fuel gas outlet (5), oxidant gas inlet ports (6), oxidant gas outlet (7) and draining Mouth (8);Wherein, the fuel gas inlet (4) on anode plate (1) and fuel gas outlet (5) with the groove on anode plate (1) (3) it is connected to;Oxidant gas inlet ports (6) and oxidant gas outlet (7) on cathode plate (2) with it is recessed on cathode plate (2) Slot (3) connection, each groove (3) is interior to be filled with porous three-dimensional substrate filling block (9).
2. dual polar plates of proton exchange membrane fuel cell according to claim 1, it is characterised in that: the interior bottom of groove (3) is in Plane setting.
3. dual polar plates of proton exchange membrane fuel cell according to claim 2, it is characterised in that: the depth of groove (3) is 0.05mm-1mm。
4. dual polar plates of proton exchange membrane fuel cell described in any one of -3 according to claim 1, it is characterised in that: porous three-dimensional Substrate filling block (9) is porous nickel screen.
5. dual polar plates of proton exchange membrane fuel cell according to claim 4, it is characterised in that: porous three-dimensional substrate filling block (9) porosity is 85%-98%.
6. dual polar plates of proton exchange membrane fuel cell according to claim 5, it is characterised in that: porous three-dimensional substrate filling block (9) with a thickness of 0.05mm-1mm.
7. dual polar plates of proton exchange membrane fuel cell according to claim 6, it is characterised in that: the outer plate surface of anode plate (1) Be all provided on inner plate surface fluted (3), the outer plate surface of cathode plate (2) is equipped with groove (3).
8. a proton exchanging film fuel battery, it is characterised in that: including multiple arranged side by side as any in claim 1-7 Proton exchange is equipped between adjacent two dual polar plates of proton exchange membrane fuel cell of dual polar plates of proton exchange membrane fuel cell described in Film (10).
9. a kind of battery pile, it is characterised in that: the left side plate (14) and right end plate (15) being oppositely arranged including two, left side plate (14) Multiple Proton Exchange Membrane Fuel Cells as claimed in claim 8 stacked are equipped between right end plate (15).
10. fuel cell pack according to claim 9, it is characterised in that: left side plate (14) be successively arranged from top to bottom with Oxidant gas input port (11), water input (12) and fuel gas input port (13) of left side plate (14) perforation, right end plate (15) the fuel gas delivery outlet (16) penetrated through with right end plate (15), water output (17) and oxidant gas delivery outlet are equipped with (18)。
CN201910815685.8A 2019-08-30 2019-08-30 Dual polar plates of proton exchange membrane fuel cell, battery and battery pile Pending CN110444785A (en)

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CN210692683U (en) * 2019-08-30 2020-06-05 湖南理工燃料电池有限公司 Proton exchange membrane fuel cell bipolar plate, cell and cell stack

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114551916A (en) * 2022-02-25 2022-05-27 深圳市氢瑞燃料电池科技有限公司 A fuel cell stack
CN116364968A (en) * 2023-02-14 2023-06-30 西部金属材料股份有限公司 Fuel cell flow field plate with porous metal distribution and collection areas

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Application publication date: 20191112