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 PDFInfo
- Publication number
- 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
- Authority
- CN
- China
- Prior art keywords
- proton exchange
- exchange membrane
- bipolar plate
- fuel cell
- contact
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 239000012528 membrane Substances 0.000 title claims abstract description 85
- 239000000446 fuel Substances 0.000 title claims abstract description 37
- 238000000034 method Methods 0.000 title claims abstract description 25
- 239000000758 substrate Substances 0.000 claims description 24
- 239000003365 glass fiber Substances 0.000 claims description 6
- 239000000463 material Substances 0.000 claims description 6
- 239000007787 solid Substances 0.000 claims description 4
- 239000011188 CEM-1 Substances 0.000 claims description 3
- 239000011190 CEM-3 Substances 0.000 claims description 3
- 101100257127 Caenorhabditis elegans sma-2 gene Proteins 0.000 claims description 3
- 229920002430 Fibre-reinforced plastic Polymers 0.000 claims description 3
- 239000002861 polymer material Substances 0.000 claims description 3
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 claims description 2
- LQBJWKCYZGMFEV-UHFFFAOYSA-N lead tin Chemical compound [Sn].[Pb] LQBJWKCYZGMFEV-UHFFFAOYSA-N 0.000 claims description 2
- 239000002184 metal Substances 0.000 abstract description 51
- 229910052751 metal Inorganic materials 0.000 abstract description 51
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 18
- 238000010586 diagram Methods 0.000 description 7
- 238000003825 pressing Methods 0.000 description 5
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 3
- 229910052802 copper Inorganic materials 0.000 description 3
- 239000010949 copper Substances 0.000 description 3
- 229910052739 hydrogen Inorganic materials 0.000 description 3
- 239000001257 hydrogen Substances 0.000 description 3
- -1 hydrogen ions Chemical class 0.000 description 3
- 238000003475 lamination Methods 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000010248 power generation Methods 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 229920000557 Nafion® Polymers 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- 238000006116 polymerization reaction Methods 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000008602 contraction Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000005304 joining Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 238000006722 reduction reaction Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Images
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
Landscapes
- Fuel Cell (AREA)
Abstract
Description
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
322第一基板 324第一金属层322
326第二金属层 330接合片326
340质子交换膜件 350第二个双极板340 Proton Exchange
352第二基板 354第三金属层352
356第四金属层 400双极板/质子交换膜组件356
420第一双极板 422第一基板420 first
424第一金属层 426第二金属层424
430接合片 440质子交换膜件430
450第二双极板 452第二基板450 second
454第三金属层 456第四金属层454
500双极板/质子交换膜组件 520第一双极板500 bipolar plate/proton
522第一基板 524电极区域522
526下表面 528导电凸起结构526
530接合片 540质子交换膜件530
550第二双极板 552第二基板550 second
554电极区域 556上表面554
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
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
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
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
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
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
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)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2008100040855A CN101241994B (en) | 2004-09-14 | 2004-09-14 | Method for Improving Contact Between Bipolar Plate and Proton Exchange Membrane of Flat Fuel Cell |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2008100040855A CN101241994B (en) | 2004-09-14 | 2004-09-14 | Method for Improving Contact Between Bipolar Plate and Proton Exchange Membrane of Flat Fuel Cell |
Related Parent Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CNB2004100747711A Division CN100375323C (en) | 2004-09-14 | 2004-09-14 | Method for improving contact between bipolar plate of flat plate type fuel cell and proton exchange membrane |
Publications (2)
Publication Number | Publication Date |
---|---|
CN101241994A true CN101241994A (en) | 2008-08-13 |
CN101241994B CN101241994B (en) | 2011-01-26 |
Family
ID=39933321
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN2008100040855A Expired - Fee Related CN101241994B (en) | 2004-09-14 | 2004-09-14 | Method for Improving Contact Between Bipolar Plate and Proton Exchange Membrane of Flat Fuel Cell |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN101241994B (en) |
Cited By (2)
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 |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
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 |
-
2004
- 2004-09-14 CN CN2008100040855A patent/CN101241994B/en not_active Expired - Fee Related
Cited By (3)
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 |
Also Published As
Publication number | Publication date |
---|---|
CN101241994B (en) | 2011-01-26 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US8609297B2 (en) | Flat fuel cell assembly and fabrication thereof | |
US7807310B2 (en) | End plate for fuel cell stack and air breathing fuel cell stack using the same | |
US20070227654A1 (en) | Method of improving the contact between bipolar plates and membrane electrode assembly of a flat panel fuel cell | |
JP2006253135A (en) | FUEL CELL STACK AND FUEL CELL SYSTEM USING FUEL CELL STACK | |
JP5130692B2 (en) | Electrochemical device and manufacturing method thereof | |
KR20050121939A (en) | Fuel cell and method for preparating the same | |
TW200532979A (en) | Flat panel direct methanol fuel cell and method of making the same | |
KR100793636B1 (en) | Unit cell for fuel cell, manufacturing method and fuel cell system | |
CN112310433B (en) | Sealing structure of fuel cell and assembly method of fuel cell stack | |
CN214254475U (en) | Fuel cell and repeating component for fuel cell | |
US7855029B2 (en) | Fuel cell module | |
CN100375323C (en) | Method for improving contact between bipolar plate of flat plate type fuel cell and proton exchange membrane | |
JP2007193948A (en) | Fuel cell | |
CN100570942C (en) | Fuel Cell Module Structure | |
CN101241994A (en) | Method for improving contact between bipolar plate of flat plate type fuel cell and proton exchange membrane | |
JP2006107868A (en) | Cell for fuel cell, its manufacturing method and fuel cell | |
JP2019139993A (en) | Fuel cell module and manufacturing method thereof | |
US20080003486A1 (en) | Current collector board for fuel cell | |
US20050191517A1 (en) | Separator and direct methanol type fuel cell therewith | |
JP4862258B2 (en) | Flat type polymer electrolyte fuel cell separator | |
CN100359731C (en) | Direct methanol fuel cell and manufacturing method of bipolar plate substrate thereof | |
JP2005251676A (en) | Separator manufacturing method | |
JP4306432B2 (en) | Fuel cell | |
JP4672492B2 (en) | Fuel cell system and stack | |
JP4826159B2 (en) | Fuel cell separator and seal molding method thereof |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C17 | Cessation of patent right | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110126 Termination date: 20130914 |