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CN101241994A - Method for improving contact between bipolar plate of flat plate type fuel cell and proton exchange membrane - Google Patents

Method for improving contact between bipolar plate of flat plate type fuel cell and proton exchange membrane Download PDF

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CN101241994A
CN101241994A CNA2008100040855A CN200810004085A CN101241994A CN 101241994 A CN101241994 A CN 101241994A CN A2008100040855 A CNA2008100040855 A CN A2008100040855A CN 200810004085 A CN200810004085 A CN 200810004085A CN 101241994 A CN101241994 A CN 101241994A
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proton exchange
exchange membrane
bipolar plate
fuel cell
contact
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CN101241994B (en
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刘永义
尚希贤
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Nanya Circuit Board Co ltd
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Nanya Circuit Board Co ltd
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    • 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
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    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells

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Abstract

The invention relates to a method for improving the contact between a bipolar plate and a proton exchange membrane of a flat plate type fuel cell. The invention utilizes the thickness variation of the metal layers on the upper and lower surfaces of the bipolar plate and provides a conductive raised structure and other methods to solve the problem of poor contact when the bipolar plate is pressed with the proton exchange membrane.

Description

改善平板式燃料电池的双极板与质子交换膜件接触的方法 Method for Improving Contact Between Bipolar Plate and Proton Exchange Membrane of Flat Fuel Cell

本发明是申请号为200410074771.1、申请日为2004年9月14日、发明名称为“改善平板式燃料电池的双极板与质子交换膜件接触的方法”的分案申请。The present invention is a divisional application with the application number 200410074771.1, the filing date is September 14, 2004, and the title of the invention is "Method for Improving Contact between Bipolar Plate and Proton Exchange Membrane of Flat Fuel Cell".

技术领域technical field

本发明是关于一种平板式燃料电池,尤指一种改善平板式燃料电池的双极电极板(或称双电极板、双极板)与质子交换膜件接触的方法。The invention relates to a flat fuel cell, in particular to a method for improving the contact between the bipolar electrode plate (or bipolar plate, bipolar plate) of the flat fuel cell and the proton exchange membrane.

背景技术Background technique

直接甲醇燃料电池(Direct Methanol Fuel Cell,DMFC)是一种利用液态的稀释甲醇水溶液或纯甲醇作为燃料,通过电化学程序将化学能转换成电力的发电装置。与传统的发电方式相较,直接甲醇燃料电池具有低污染、低噪音、高能量密度以及较高的能量转换效率等优点,乃具有前瞻性的干净能源,可应用的领域包括家用发电系统、电子产品、运输工具、军用设备、太空工业等。Direct Methanol Fuel Cell (DMFC) is a power generation device that uses liquid dilute methanol aqueous solution or pure methanol as fuel to convert chemical energy into electricity through an electrochemical process. Compared with traditional power generation methods, direct methanol fuel cells have the advantages of low pollution, low noise, high energy density, and high energy conversion efficiency. Products, vehicles, military equipment, space industry, etc.

直接甲醇燃料电池的运作原理乃以甲醇水溶液在阳极触媒层进行氧化反应,产生氢离子(H+)、电子(e-)以及二氧化碳(CO2),其中氢离子经由电解质传递至阴极,而电子经由外部电路传递至负载作功后再传递至阴极,此时供给阴极端的氧气会与氢离子及电子在阴极触媒层进行还原反应,并产生水。The operating principle of the direct methanol fuel cell is that the methanol aqueous solution is oxidized on the anode catalyst layer to generate hydrogen ions (H + ), electrons (e - ) and carbon dioxide (CO 2 ), in which the hydrogen ions are transferred to the cathode through the electrolyte, and the electrons It is transmitted to the load through an external circuit and then transmitted to the cathode. At this time, the oxygen supplied to the cathode will undergo a reduction reaction with hydrogen ions and electrons in the cathode catalyst layer to produce water.

燃料电池一般皆由数个基本单元所组成。由于每个基本单元所能提供的电压较小,因此在应用时必须串联多的基本单元,以达到所需要的操作电压输出。Fuel cells are generally composed of several basic units. Since the voltage that each basic unit can provide is relatively small, many basic units must be connected in series in order to achieve the required operating voltage output.

发明内容Contents of the invention

本发明的主要目的在提供一种改善平板式燃料电池的双极板与质子交换膜件接触的方法,以解决习知技艺的缺点。The main purpose of the present invention is to provide a method for improving the contact between the bipolar plate and the proton exchange membrane of the flat fuel cell, so as to solve the disadvantages of the prior art.

为达上述目的,本发明提供一种改善平板式燃料电池的双极板与质子交换膜件接触的方法,包含有下列步骤:In order to achieve the above object, the present invention provides a method for improving the contact between the bipolar plate of the flat fuel cell and the proton exchange membrane, comprising the following steps:

提供一第一双极板、一质子交换膜件、一第二双极板以及至少一接合片,其中质子交换膜件放置于第一双极板上,接合片具有一用以容置质子交换膜件的开口处,而第二双极板置于质子交换膜件上,其中第一双极板具有一与质子交换膜件接触的第一质子交换面以及一接触燃料的燃料面,第二双极板具有一与质子交换膜件接触的第二质子交换面以及一接触空气的空气面,其中燃料面上设有第一金属层、第一质子交换面上设有第二金属层、该第二质子交换面上设有第三金属层以及该空气面上设有第四金属层,其中该第二金属层的厚度大于该第一金属层的厚度,该第三金属层的厚度大于该第四金属层的厚度;Provide a first bipolar plate, a proton exchange membrane member, a second bipolar plate and at least one junction piece, wherein the proton exchange membrane member is placed on the first bipolar plate, and the junction piece has a The opening of the membrane, and the second bipolar plate is placed on the proton exchange membrane, wherein the first bipolar plate has a first proton exchange surface in contact with the proton exchange membrane and a fuel surface contacting the fuel, the second The bipolar plate has a second proton exchange surface in contact with the proton exchange membrane and an air surface in contact with air, wherein the fuel surface is provided with a first metal layer, the first proton exchange surface is provided with a second metal layer, the A third metal layer is provided on the second proton exchange surface and a fourth metal layer is provided on the air surface, wherein the thickness of the second metal layer is greater than the thickness of the first metal layer, and the thickness of the third metal layer is greater than the thickness of the the thickness of the fourth metal layer;

其中,该第一双极板包含有一第一基板,其上形成该第一金属层和该第二金属层;该第二双极板包含有一第二基板,其上形成该第三金属层和该第四金属层;该质子交换膜件中的质子交换膜为固态质子交换膜;Wherein, the first bipolar plate includes a first substrate on which the first metal layer and the second metal layer are formed; the second bipolar plate includes a second substrate on which the third metal layer and the second metal layer are formed. The fourth metal layer; the proton exchange membrane in the proton exchange membrane is a solid proton exchange membrane;

然后将第一双极板、质子交换膜件、第二双极板以及该接合片压合,成双极板/质子交换膜组件。Then press the first bipolar plate, the proton exchange membrane element, the second bipolar plate and the joining piece to form a bipolar plate/proton exchange membrane assembly.

本发明提供另一种改善平板式燃料电池的双极板与质子交换膜件接触的方法,包含有下列步骤,提供一双极板以及一质子交换膜件,其中双极板包含有至少一电极区域,质子交换膜件欲置于双极板的电极区域上,于电极区域上提供多个导电凸起结构,以及将质子交换膜件与多个导电凸起结构接触。The present invention provides another method for improving the contact between the bipolar plate and the proton exchange membrane of a flat fuel cell, comprising the following steps, providing a bipolar plate and a proton exchange membrane, wherein the bipolar plate includes at least one electrode region The proton exchange membrane is to be placed on the electrode area of the bipolar plate, a plurality of conductive protrusion structures are provided on the electrode area, and the proton exchange membrane is in contact with the plurality of conductive protrusion structures.

附图说明Description of drawings

图1显示习知技艺的平板式燃料电池的双极板/质子交换膜组件示意图;Fig. 1 shows the schematic diagram of the bipolar plate/proton exchange membrane assembly of the planar fuel cell of prior art;

图2显示习知技艺的平板式燃料电池的双极板/质子交换膜组件压合后示意图;Fig. 2 shows the schematic diagram after pressing the bipolar plate/proton exchange membrane assembly of the flat fuel cell of the prior art;

图3显示本发明较佳实施例的平板式燃料电池的双极板/质子交换膜组件示意图;Fig. 3 shows the schematic diagram of the bipolar plate/proton exchange membrane assembly of the planar fuel cell of preferred embodiment of the present invention;

图4显示本发明较佳实施例的平板式燃料电池的双极板/质子交换膜组件压合后示意图;Fig. 4 shows the schematic diagram after pressing the bipolar plate/proton exchange membrane assembly of the flat fuel cell of the preferred embodiment of the present invention;

图5显示本发明另一较佳实施例的平板式燃料电池的双极板/质子交换膜组件示意图;Fig. 5 shows the schematic diagram of the bipolar plate/proton exchange membrane assembly of the flat fuel cell of another preferred embodiment of the present invention;

图6显示本发明另一较佳实施例的平板式料电池的双极板/质子交换膜组件压合后示意图。FIG. 6 shows a schematic diagram of a bipolar plate/proton exchange membrane assembly of a flat-plate battery according to another preferred embodiment of the present invention after lamination.

符号说明:Symbol Description:

300双极板/质子交换膜组件 320第一个双极板300 bipolar plate/proton exchange membrane module 320 first bipolar plate

322第一基板              324第一金属层322 first substrate 324 first metal layer

326第二金属层            330接合片326 second metal layer 330 bonding piece

340质子交换膜件          350第二个双极板340 Proton Exchange Membrane 350 Second Bipolar Plate

352第二基板              354第三金属层352 second substrate 354 third metal layer

356第四金属层            400双极板/质子交换膜组件356 fourth metal layer 400 bipolar plate/proton exchange membrane module

420第一双极板            422第一基板420 first bipolar plate 422 first substrate

424第一金属层            426第二金属层424 first metal layer 426 second metal layer

430接合片                440质子交换膜件430 splicing piece 440 proton exchange membrane

450第二双极板            452第二基板450 second bipolar plate 452 second substrate

454第三金属层            456第四金属层454 third metal layer 456 fourth metal layer

500双极板/质子交换膜组件 520第一双极板500 bipolar plate/proton exchange membrane module 520 first bipolar plate

522第一基板              524电极区域522 first substrate 524 electrode area

526下表面                528导电凸起结构526 lower surface 528 conductive raised structure

530接合片                540质子交换膜件530 bonding piece 540 proton exchange membrane

550第二双极板     552第二基板550 second bipolar plate 552 second substrate

554电极区域       556上表面554 electrode area 556 upper surface

558导电凸起结构558 conductive bump structure

具体实施方式Detailed ways

请参考图1以及图2,图1以及图2分别显示平板式燃料电池的双极板与质子交换膜件压合前、后的示意图。如图1所示,平板式燃料电池的双极板/质子交换膜组件300包含有第一个双极板(Bipolar Plate)320、至少一接合片(Bonding sheet)330、一质子交换膜件(膜电极组件,Membrane Electrode Assembly,MEA)340以及第二个双极板(BipolarPlate)350。其中,第一双极板320包括一第一基板322,以及覆盖于第一基板322的上表面的第一金属层324以及下表面的第二金属层326,而第二双极板350包括一第二基板352以及覆盖于第二基板的上表面的第三金属层354以及下表面的第四金属层356,其中上述的金属层厚度均相等。前述的第一金属层324、第二金属层326、第三金属层354与第四金属层356可以是由金属铜层所构成。Please refer to FIG. 1 and FIG. 2 . FIG. 1 and FIG. 2 respectively show schematic diagrams before and after lamination of the bipolar plate and the proton exchange membrane of the flat fuel cell. As shown in Figure 1, the bipolar plate/proton exchange membrane assembly 300 of flat fuel cell comprises the first bipolar plate (Bipolar Plate) 320, at least one bonding sheet (Bonding sheet) 330, a proton exchange membrane ( Membrane Electrode Assembly, Membrane Electrode Assembly, MEA) 340 and a second bipolar plate (BipolarPlate) 350. Wherein, the first bipolar plate 320 includes a first substrate 322, a first metal layer 324 covering the upper surface of the first substrate 322 and a second metal layer 326 on the lower surface, and the second bipolar plate 350 includes a The second substrate 352 , the third metal layer 354 covering the upper surface of the second substrate, and the fourth metal layer 356 covering the lower surface of the second substrate, wherein the metal layers mentioned above have the same thickness. The aforementioned first metal layer 324 , second metal layer 326 , third metal layer 354 and fourth metal layer 356 may be composed of a metal copper layer.

然后进行压合制程,如图2所示,其中第二金属层326以及第三金属层354与质子交换膜件340接触,但由于金属层应力的影响,使第二金属层326以及第三金属层354与质子交换膜件340之间产生间距且附着力差等现象,甚至于质子交换膜件340因受压程度不同,造成厚度不一致、表面产生波纹以及因加热或冷却造成膨胀或收缩而与双极板分离等情形产生。由于前述双极板/质子交换膜组件300压合后所产生的现象,造成制程成本提高、良率降低等现象。Then carry out the pressing process, as shown in Figure 2, wherein the second metal layer 326 and the third metal layer 354 are in contact with the proton exchange membrane member 340, but due to the influence of the stress of the metal layer, the second metal layer 326 and the third metal layer Between the layer 354 and the proton exchange membrane member 340 there is a gap and poor adhesion, and even the proton exchange membrane member 340 is not uniform in thickness due to different degrees of pressure, ripples are generated on the surface, and expansion or contraction is caused by heating or cooling. Separation of bipolar plates, etc. occurs. Due to the phenomena that occur after the aforementioned bipolar plate/proton exchange membrane module 300 is pressed together, the process cost increases and the yield rate decreases.

因此本发明提供一种改善平板式燃料电池的双极板与质子交换膜件接触的制造方法,以解决前述的问题。Therefore, the present invention provides a manufacturing method for improving the contact between the bipolar plate and the proton exchange membrane of the flat fuel cell, so as to solve the aforementioned problems.

请参阅图3与图4,图3与图4显示本发明较佳实施例的改善平板式燃料电池的双极板与质子交换膜件接触的制造方法。如图3所示,平板式燃料电池的双极板/质子交换膜组件400包含有第一双极板(BipolarPlate)420、至少一接合片(Bonding sheet)430、一质子交换膜件(膜电极组件,Membrane Electrode Assembly,MEA)440以及第二双极板(Bipolar Plate)450。其中,第一双极板420包括一第一基板422,其上表面设有第一金属层424以及下表面设有第二金属层426,而第二双极板450包括一第二基板452,其上表面设有第三金属层454以及下表面设有第四金属层456。前述的第一金属层424、第二金属层426、第三金属层454与第四金属层456可以是由金属铜层所构成。其中,第二金属层426的厚度大于第一金属层424的厚度,第三金属层454的厚度大于第四金属层456的厚度,另外第一基板422以及第二基板452可以为玻纤强化高分子材料(Glass Fiber Reinforced Polymeric Material)所构成,如ANSI级的FR-1、FR-2、FR-3、FR-4、FR-5、CEM-1或CEM-3等等所构成,而质子交换膜件中的质子交换膜可采用如杜邦公司Nafion质子交换膜,或具有相同功能的其它固态质子交换膜,另外接合片可以为因双电路板制程中所用的部分聚合阶段(B-stage)的“PREPREG”树脂胶片等材质。Please refer to FIG. 3 and FIG. 4 . FIG. 3 and FIG. 4 show a manufacturing method for improving the contact between the bipolar plate and the proton exchange membrane of a flat fuel cell according to a preferred embodiment of the present invention. As shown in Figure 3, the bipolar plate/proton exchange membrane assembly 400 of the planar fuel cell comprises a first bipolar plate (BipolarPlate) 420, at least one bonding sheet (Bonding sheet) 430, a proton exchange membrane (membrane electrode) Components, Membrane Electrode Assembly, MEA) 440 and a second bipolar plate (Bipolar Plate) 450. Wherein, the first bipolar plate 420 includes a first substrate 422 with a first metal layer 424 on its upper surface and a second metal layer 426 on its lower surface, and the second bipolar plate 450 includes a second substrate 452, A third metal layer 454 is provided on the upper surface and a fourth metal layer 456 is provided on the lower surface. The aforementioned first metal layer 424 , second metal layer 426 , third metal layer 454 and fourth metal layer 456 may be composed of a metal copper layer. Wherein, the thickness of the second metal layer 426 is greater than the thickness of the first metal layer 424, the thickness of the third metal layer 454 is greater than the thickness of the fourth metal layer 456, and the first substrate 422 and the second substrate 452 can be glass fiber reinforced high Molecular material (Glass Fiber Reinforced Polymeric Material), such as ANSI grade FR-1, FR-2, FR-3, FR-4, FR-5, CEM-1 or CEM-3, etc., and proton The proton exchange membrane in the exchange membrane can be used such as DuPont's Nafion proton exchange membrane, or other solid proton exchange membranes with the same function. In addition, the bonding piece can be part of the polymerization stage (B-stage) used in the double circuit board process. "PREPREG" resin film and other materials.

然后进行压合制程,如图4所示,将第一双极板420、质子交换膜件440、第二双极板450以及接合片430压合,构成双极板/质子交换膜组件400。Then a pressing process is performed. As shown in FIG. 4 , the first bipolar plate 420 , the proton exchange membrane element 440 , the second bipolar plate 450 and the bonding piece 430 are pressed together to form the bipolar plate/proton exchange membrane assembly 400 .

请参阅图5与图6,图5与图6显示本发明另一较佳实施例的改善平板式燃料电池的双极板与质子交换膜件接触的制造方法。如图5所示,平板式燃料电池的双极板/质子交换膜组件500包含有第一双极板(Bipolar Plate)520、至少一接合片(Bonding sheet)530、一质子交换膜件(膜电极组件,Membrane Electrode Assembly,MEA)540以及第二双极板(Bipolar Plate)550。第一双极板520包含有第一基板522以及至少一电极区域524,接着于电极区域524的下表面526上提供多个导电凸起(bump)结构528,而第二双极板550包含有第二基板552以及至少一电极区域554,随后于电极区域554的上表面556上提供多个导电凸起结构558。其中,导电凸起结构528、558可以为锡、铅、锡铅或铜所构成,最外层则覆盖以镀金层,且导电凸起结构528、558的高度可大于0.1mm。而质子交换膜件540欲置于第一双极板520的电极区域524以及第二双极板550的电极区域554之间。其中第一基板522以及第二基板552可以为玻纤强化高分子材料(Glass Fiber Reinforced Polymeric Material)所构成,如ANSI级的FR-1、FR-2、FR-3、FR-4、FR-5、CEM-1或CEM-3等等所构成,另外质子交换膜件中的质子交换膜可采用如杜邦公司Nafion质子交换膜,或具有相同功能的其它固态质子交换膜,而接合片可以为因双电路板制程中所用的部分聚合阶段(B-stage)的“PREPREG”树脂胶片等材质。Please refer to FIG. 5 and FIG. 6 . FIG. 5 and FIG. 6 show another preferred embodiment of the present invention, a manufacturing method for improving the contact between the bipolar plate and the proton exchange membrane of the flat fuel cell. As shown in Figure 5, the bipolar plate/proton exchange membrane assembly 500 of the flat fuel cell comprises a first bipolar plate (Bipolar Plate) 520, at least one bonding sheet (Bonding sheet) 530, a proton exchange membrane (membrane) Electrode assembly, Membrane Electrode Assembly, MEA) 540 and a second bipolar plate (Bipolar Plate) 550. The first bipolar plate 520 includes a first substrate 522 and at least one electrode region 524, and then provides a plurality of conductive bump structures 528 on the lower surface 526 of the electrode region 524, and the second bipolar plate 550 includes The second substrate 552 and at least one electrode region 554 are provided with a plurality of conductive protrusion structures 558 on the upper surface 556 of the electrode region 554 . Wherein, the conductive protruding structures 528, 558 can be made of tin, lead, tin-lead or copper, and the outermost layer is covered with a gold-plated layer, and the height of the conductive protruding structures 528, 558 can be greater than 0.1 mm. The proton exchange membrane element 540 is intended to be placed between the electrode area 524 of the first bipolar plate 520 and the electrode area 554 of the second bipolar plate 550 . Wherein the first substrate 522 and the second substrate 552 can be made of glass fiber reinforced polymer material (Glass Fiber Reinforced Polymeric Material), such as ANSI grade FR-1, FR-2, FR-3, FR-4, FR- 5. Composed of CEM-1 or CEM-3, etc. In addition, the proton exchange membrane in the proton exchange membrane can be used such as DuPont Nafion proton exchange membrane, or other solid proton exchange membranes with the same function, and the joint piece can be Due to the partial polymerization stage (B-stage) "PREPREG" resin film and other materials used in the double circuit board process.

接着进行压合制程,如图6所示,将第一双极板520、质子交换膜件540、第二双极板550以及接合片530压合,构成双极板/质子交换膜组件500。Then a pressing process is performed. As shown in FIG. 6 , the first bipolar plate 520 , the proton exchange membrane element 540 , the second bipolar plate 550 and the bonding sheet 530 are pressed together to form the bipolar plate/proton exchange membrane assembly 500 .

综上所述,本发明改善平板式燃料电池的双极板与质子交换膜件接触的方法相较于习知技艺至少包括以下的优点:In summary, compared with the prior art, the method for improving the contact between the bipolar plate and the proton exchange membrane of the flat fuel cell of the present invention at least includes the following advantages:

平板式燃料电池的双极板采用不同厚度的上下金属层或是于面对质子交换膜件单元的电极区域表面采用导电凸起结构,不但可降低因为质子交换膜件单元本身厚度不均匀,而且压合后厚度会减少,因而使得双极板与质子交换膜件单元二者间无法完全接触的缺点,还可特别对质子交换膜件单元施以适当的压力,以提高发电量。The bipolar plate of the flat fuel cell adopts upper and lower metal layers of different thicknesses or adopts a conductive convex structure on the surface of the electrode area facing the proton exchange membrane unit, which can not only reduce the uneven thickness of the proton exchange membrane unit itself, but also The thickness will be reduced after lamination, so that the bipolar plate and the proton exchange membrane unit cannot be fully contacted, and the proton exchange membrane unit can also be properly pressured to increase the power generation.

Claims (7)

1.一种改善平板式燃料电池的双电极板与质子交换膜件接触的方法,包含有:1. A method for improving the contact between a double-electrode plate of a flat fuel cell and a proton exchange membrane, comprising: 提供一双极板以及一质子交换膜件,其中该双极板包含有至少一电极区域,该质子交换膜件欲置于该双极板的该电极区域上;providing a bipolar plate and a proton exchange membrane element, wherein the bipolar plate includes at least one electrode region, and the proton exchange membrane element is to be placed on the electrode region of the bipolar plate; 于该电极区域上提供多个导电凸起结构;providing a plurality of conductive protrusion structures on the electrode area; 将该质子交换膜件与该多个导电凸起结构接触。The proton exchange membrane is in contact with the plurality of conductive protrusion structures. 2.根据权利要求1所述的一种改善平板式燃料电池的双电极板与质子交换膜件接触的方法,其中该多个导电凸起结构的高度不小于0.1mm。2. A method for improving the contact between the double-electrode plate and the proton exchange membrane of a flat fuel cell according to claim 1, wherein the height of the plurality of conductive protrusion structures is not less than 0.1 mm. 3.根据权利要求1所述的一种改善平板式燃料电池的双电极板与质子交换膜件接触的方法,其中该导电凸起结构由包含锡、铅、锡铅材料所构成。3. A method for improving the contact between the double-electrode plate and the proton exchange membrane of a flat fuel cell according to claim 1, wherein the conductive protrusion structure is made of materials including tin, lead, and tin-lead. 4.根据权利要求1所述的一种改善平板式燃料电池的双电极板与质子交换膜件接触的方法,其中该质子交换膜件中的质子交换膜为固态质子交换膜。4. A method for improving the contact between the double-electrode plate of the flat fuel cell and the proton exchange membrane according to claim 1, wherein the proton exchange membrane in the proton exchange membrane is a solid proton exchange membrane. 5.根据权利要求1所述的一种改善平板式燃料电池的双电极板与质子交换膜件接触的方法,其中该双极板包含有一基板,其上形成该电极区域。5. A method for improving the contact between a bipolar plate of a flat fuel cell and a proton exchange membrane according to claim 1, wherein the bipolar plate comprises a substrate on which the electrode region is formed. 6.根据权利要求5所述的一种改善平板式燃料电池的双电极板与质子交换膜件接触的方法,其中该基板为玻纤强化高分子材料所构成。6 . The method for improving the contact between the double-electrode plate and the proton exchange membrane of a flat fuel cell according to claim 5 , wherein the substrate is made of glass fiber reinforced polymer material. 7.根据权利要求5所述的一种改善平板式燃料电池的双电极板与质子交换膜件接触的方法,其中该基板为ANSI级的FR-1、FR-2、FR-3、FR-4、FR-5、CEM-1或CEM-3的玻纤强化高分子材料所构成。7. A kind of method for improving the double-electrode plate of flat-plate fuel cell according to claim 5 and proton exchange membrane part contacts, and wherein this substrate is the FR-1 of ANSI level, FR-2, FR-3, FR- 4. Made of FR-5, CEM-1 or CEM-3 glass fiber reinforced polymer materials.
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CN108407099A (en) * 2018-02-07 2018-08-17 广东国鸿氢能科技有限公司 Graphite bi-polar plate flattens machine frame
CN112952168A (en) * 2019-12-11 2021-06-11 中国科学院大连化学物理研究所 Flattening method and device for fuel cell proton exchange membrane

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DE4120359C2 (en) * 1990-06-21 1993-11-18 Deutsche Aerospace Process for the production of an electrochemical cell and its use
CN1462172A (en) * 2002-05-27 2003-12-17 联测科技股份有限公司 Printed circuit board with fixed solder mask
CN1501533B (en) * 2002-11-14 2012-01-04 钟发平 Method for making a lead fabric battery using novel lead fabric as polar plate grid

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108407099A (en) * 2018-02-07 2018-08-17 广东国鸿氢能科技有限公司 Graphite bi-polar plate flattens machine frame
CN112952168A (en) * 2019-12-11 2021-06-11 中国科学院大连化学物理研究所 Flattening method and device for fuel cell proton exchange membrane
CN112952168B (en) * 2019-12-11 2023-04-18 中国科学院大连化学物理研究所 Flattening method and device for fuel cell proton exchange membrane

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