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CN1416184A - Metal compound bipolar plate of fuel cell with proton exchange film - Google Patents

Metal compound bipolar plate of fuel cell with proton exchange film Download PDF

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CN1416184A
CN1416184A CN01132483A CN01132483A CN1416184A CN 1416184 A CN1416184 A CN 1416184A CN 01132483 A CN01132483 A CN 01132483A CN 01132483 A CN01132483 A CN 01132483A CN 1416184 A CN1416184 A CN 1416184A
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metal
bipolar plate
plate
strip
boss
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史鹏飞
杜春雨
尹鸽平
程新群
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Harbin Institute of Technology Shenzhen
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Harbin Institute of Technology Shenzhen
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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
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries
    • 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

本发明提出一种质子交换膜燃料电池的金属复合双极板,该双极板由两部分组成,一部分是与三合一电极相对应的条状沟槽部分,由两块形状完全对称的薄金属焊合而成,条状沟槽的凸台呈蛇型,另一部分是金属边框,它的作用是支撑和固定条状沟槽部分并形成气道和水道,边框和条状沟槽部分通过粘合或焊合成一体。本发明具有以下优点:1.气道可以保证燃料气、氧化剂气体的均匀分布;2.条装沟槽的凸台可以保证电流的均匀分布,最大限度地降低接触电阻;3.水冷功能可以保证电堆温度的均匀分布;4.双极板由条状沟槽部分和金属边框两部分组成既可以使其具有多项功能又有足够的机械强度。

Figure 01132483

The present invention proposes a metal composite bipolar plate for a proton exchange membrane fuel cell. The bipolar plate is composed of two parts, one part is a strip-shaped groove part corresponding to the three-in-one electrode, and two completely symmetrical thin It is made of metal welding, the boss of the strip groove is snake-shaped, and the other part is the metal frame, which is used to support and fix the strip groove part and form the air channel and water channel. The frame and the strip groove part pass through Bonded or welded into one. The invention has the following advantages: 1. The gas channel can ensure the uniform distribution of fuel gas and oxidant gas; 2. The boss with strip groove can ensure the uniform distribution of current and minimize the contact resistance; 3. The water cooling function can ensure Uniform distribution of stack temperature; 4. The bipolar plate is composed of two parts, a strip groove part and a metal frame, which can not only make it have multiple functions but also have sufficient mechanical strength.

Figure 01132483

Description

质子交换膜燃料电池的金属复合双极板Metal Composite Bipolar Plates for Proton Exchange Membrane Fuel Cells

技术领域:Technical field:

本发明提出一种质子交换膜燃料电池的金属复合双极板,属于燃料电池技术领域。The invention provides a metal composite bipolar plate of a proton exchange membrane fuel cell, which belongs to the technical field of fuel cells.

背景技术:Background technique:

燃料电池是一种可将化学能连续不断地直接转变为电能的发电装置。当电池工作时,要连续不断地向电池内输送燃料和氧化剂即可连续不断地得到电能,同时要连续不断地排除化学反应的产物水的同时还要连续不断地排除因化学反应产生的热。由于质子交换膜燃料电池有工作温度低、启动快、能量转化效率高、与环境友好等特点,开发质子交换膜燃料电池成为现代科技攻关的热点之一。但是,以目前的技术水平质子交换膜燃料电池还无法实现商业化,其中一个非常主要的因素就是双极板。双极板的材料、流场结构,尤其是其加工成本(目前的技术水平,双极板的成本要占整个燃料电池成本的40%~60%以上)都存在许多亟待解决的技术问题。目前,世界上在这方面的研究工作进行的很多。主要的研究方向有:碳-聚合物复合材料和金属基材料。碳-聚合物复合材料的研究主要是将石墨与聚合物材料经一定方式混合,然后经冲压成型。其中石墨材料起导电作用,而聚合物起粘接作用。这种方式能够较大程度降低生产成本,但石墨的添加量不能过大,否则会降低材料的可冲压性,还造成石墨分布不均,容易产生气体的渗漏,而且使得材料的导电性比本来就比金属差的石墨更低。而金属基材料双极板由于良好的导电性、机械强度和低成本则成为研究热点,对金属基双极板材料的研究一方向集中在材料的简单替代上,另一方面则侧重开发新的高效低成本结构。在现有技术中,一种是采用了厚度只有零点几个毫米的钛金属板作为基材,制备出兼具冷却板的功能的新型双极板。首先将薄钛板用冲压等方法加工出沟槽结构,然后用钎焊的方法将两个金属薄板直接,或者通过一中间金属隔板焊接起来。金属板表面的沟槽作为气体通道,而两个金属板的中间腔体则构成液体冷却剂的通道。这种方法可以将双极板做得很轻,散热良好。但是采用钛材料其成本仍较高。另一种是采用厚度只有0.2~0.3毫米的薄金属板,如不锈钢(钢号310或316,其中310双极板比316双极板表现出更好的极化特性),来做双极板材料,流场板则采用方形的不锈钢等金属筛网,进气孔和出气孔分别位于流场板的对角线上,可以保证相对均匀的气流分布。冷却板的形式与双极板类似,在两个较薄(厚度为0.25mm左右)的金属板中间夹以一金属网,液体冷却剂从金属网中流过以保证良好的流体分布,整个冷却板的厚度为3毫米。第三种是由三层薄金属板构成的燃料电池双极板,中间为分隔板,两侧为带有条状沟槽的导流板。导流板上的沟槽由入口到出口是连续的;并且沟槽之间逐渐并接,使得沟槽的横截面积由气体入口到出口逐级衰减,条状沟槽占整个工作面积的1/2~4/5。以上技术都是从某一个侧面来改善双极板的性能,但是没有一个将减轻双极板的体积和重量,改善反应气体的利用率,增加双极板的冷却功能,提高双极板材料的导电性,降低材料与生产成本以及具有良好的装配性等各方面综合考虑并包容进去的,因此他们对双极板性能和成本的改进都是不全面的,都只是在某一方面有提高。A fuel cell is a power generating device that can continuously and directly convert chemical energy into electrical energy. When the battery is working, it is necessary to continuously deliver fuel and oxidant to the battery to obtain electrical energy continuously, and at the same time, it is necessary to continuously remove the water produced by the chemical reaction and the heat generated by the chemical reaction. Because proton exchange membrane fuel cells have the characteristics of low operating temperature, fast start-up, high energy conversion efficiency, and environmental friendliness, the development of proton exchange membrane fuel cells has become one of the hotspots of modern scientific and technological research. However, proton exchange membrane fuel cells cannot be commercialized at the current technical level, and one of the most important factors is the bipolar plate. The material of the bipolar plate, the structure of the flow field, and especially its processing cost (at the current technical level, the cost of the bipolar plate accounts for more than 40% to 60% of the cost of the entire fuel cell) all have many technical problems to be solved urgently. At present, there are many researches in this field in the world. The main research directions are: carbon-polymer composite materials and metal-based materials. The research of carbon-polymer composite materials is mainly to mix graphite and polymer materials in a certain way, and then press them into shape. Among them, the graphite material plays a conductive role, while the polymer plays a bonding role. This method can reduce the production cost to a large extent, but the amount of graphite added should not be too large, otherwise it will reduce the stampability of the material, and cause uneven distribution of graphite, which is prone to gas leakage, and makes the conductivity of the material lower than Graphite, which is inherently inferior to metals, is lower. The metal-based bipolar plate has become a research hotspot due to its good electrical conductivity, mechanical strength and low cost. The research on metal-based bipolar plate materials focuses on the simple substitution of materials on the one hand, and on the other hand focuses on the development of new High efficiency and low cost structure. In the prior art, one is to use a titanium metal plate with a thickness of only a few tenths of a millimeter as a base material to prepare a new type of bipolar plate with the function of a cooling plate. First, the thin titanium plate is processed into a groove structure by stamping and other methods, and then the two metal thin plates are welded directly or through an intermediate metal partition by brazing. Grooves on the surface of the metal plates act as gas channels, while the cavity in the middle of the two metal plates forms the channel for the liquid coolant. This method can make the bipolar plate very light and has good heat dissipation. However, the cost of using titanium materials is still relatively high. The other is to use a thin metal plate with a thickness of only 0.2 to 0.3 mm, such as stainless steel (steel grade 310 or 316, of which 310 bipolar plates have better polarization characteristics than 316 bipolar plates) to make bipolar plates Material, the flow field plate is made of square stainless steel and other metal screens, and the air inlet and outlet holes are located on the diagonal of the flow field plate, which can ensure a relatively uniform air flow distribution. The form of the cooling plate is similar to that of a bipolar plate. A metal mesh is sandwiched between two thinner metal plates (thickness is about 0.25mm). The liquid coolant flows through the metal mesh to ensure good fluid distribution. The entire cooling plate The thickness is 3 mm. The third type is a fuel cell bipolar plate composed of three layers of thin metal plates, with a separator in the middle and deflectors with strip grooves on both sides. The grooves on the deflector are continuous from the inlet to the outlet; and the grooves are gradually joined together, so that the cross-sectional area of the grooves gradually decreases from the gas inlet to the outlet, and the strip grooves account for 1% of the entire working area. /2~4/5. The above technologies all improve the performance of the bipolar plate from a certain side, but none of them will reduce the volume and weight of the bipolar plate, improve the utilization rate of the reaction gas, increase the cooling function of the bipolar plate, and improve the stability of the bipolar plate material. Conductivity, reduction of material and production costs, and good assembly are comprehensively considered and included. Therefore, their improvements to the performance and cost of bipolar plates are not comprehensive, and they are only improved in one aspect.

发明内容:Invention content:

本发明由两部分组成,一部分是与三合一电极相对应的条状沟槽部分。这一部分由两块形状完全对称的薄金属板焊合而成,其要点是:条状沟槽的凸台呈蛇型,共有两个特点:一是将气体导流槽分割为两个彼此不相通的梳型气道,这两个彼此不相通的梳型气道一个是进气道一个是排气道;另一个特点是两块形状完全对称的薄金属板上的呈蛇行的条状沟槽的凸台构成了一蛇型的冷却水道;另一部分是金属边框,它的作用是支撑和固定条状沟槽部分并形成气道和水道。边框和条状沟槽部分通过粘合或焊合成一体。下面结合附图详细阐述本发明原理和结构:金属边框1中间,镶有两块结构、形状完全对称的薄金属板2,上薄金属板为阳极板,下薄金属板为阴极板,阳极板和阴极板焊接成一个整体,在金属边框1两下角处钻有圆孔3、4,在金属边框1两上角处分别钻有方孔7、8和圆孔5、6,在圆孔4、6处加工凹槽与蛇型条状沟槽构成气体通道,方孔7、8处加工出凹槽与两极板间的蛇型冷却剂通道相连,在阳极板上经冲压,制成呈蛇型的条状沟槽凸台,在呈蛇型条状沟槽的凸台内部构成了一条蛇型的冷却剂通道,可以通过控制冷却剂流量和流速来严格控制燃料电池的内部温度,有利于反应区域的温度及电流密度均匀分布,提高燃料电池的性能。本发明中呈蛇型的条状沟槽凸台将气体导流槽分割为两个彼此不相通的梳型气道,燃料气、氧化剂气体分别通过各自的梳型进气道到达凸台的一侧,然后沿与凸台垂直的方向通过扩散层流到排气道。该结构可以充分地保证气体均匀地到达电极的每一个角落,提高反应气体的利用率。由于氧化剂气体从进气孔必须通过蛇行通道的凸台才能够到达对角线一侧的出气孔,这种气体流动方式有利于燃料电池阴极一侧的产物水的排出。在阳、阴两块极板的凸起表面,镀有Ag和Au等金属,可有效改善两个极板的防腐,导电或排气性能。金属边框1可用Al、不锈钢等金属制成。金属边框的作用可以起支撑和固定条状沟槽部分的作用,改善了薄不锈钢极板机械强度差的缺点,能够实现燃料电池堆的顺利安装,同时可以形成容易加工的气道和冷却剂通道。本发明将充分地发挥双极板的如下功能:1、气道可以保证燃料气、氧化剂气体的均匀分布;2、条状沟槽的凸台可以保证电流的均匀分布,最大限度地降低接触电阻;3、水冷功能可以保证电堆温度的均匀分布;4、双极板由条状沟槽部分和金属边框两部分组成既可以使其具有多项功能又有足够的机械强度。The invention consists of two parts, one part is the strip groove part corresponding to the three-in-one electrode. This part is welded by two thin metal plates with completely symmetrical shapes. The main points are: the boss of the strip groove is in the shape of a snake, and has two characteristics: one is to divide the gas diversion groove into two different parts. Comb-shaped air passages that communicate with each other, one of the two comb-shaped air passages that are not connected to each other is the intake passage and the other is the exhaust passage; the other feature is the serpentine strip grooves on two thin metal plates that are completely symmetrical in shape The boss of the groove forms a snake-shaped cooling water channel; the other part is a metal frame, which is used to support and fix the strip groove part and form an air channel and a water channel. The frame and the strip groove part are integrated by bonding or welding. Elaborate the principle of the present invention and structure below in conjunction with accompanying drawing: in the middle of metal frame 1, be inlaid with two thin metal plates 2 of structure, shape complete symmetry, upper thin metal plate is anode plate, lower thin metal plate is cathode plate, anode plate It is welded into a whole with the cathode plate, round holes 3, 4 are drilled at the two lower corners of the metal frame 1, square holes 7, 8 and round holes 5, 6 are respectively drilled at the two upper corners of the metal frame 1, and round holes 4 , 6 processing grooves and snake-shaped strip grooves form gas channels, square holes 7 and 8 processing grooves are connected with snake-shaped coolant channels between the two pole plates, and are stamped on the anode plate to form a snake The boss with strip-shaped grooves forms a serpentine coolant channel inside the boss with snake-shaped strip grooves, which can strictly control the internal temperature of the fuel cell by controlling the flow and velocity of the coolant, which is beneficial to The temperature and current density of the reaction area are evenly distributed, which improves the performance of the fuel cell. In the present invention, the snake-shaped strip-shaped groove boss divides the gas guide groove into two comb-shaped air passages that are not connected to each other, and the fuel gas and oxidant gas reach one of the bosses through their respective comb-shaped inlet passages. side, and then flow through the diffusion layer to the exhaust channel in the direction perpendicular to the boss. This structure can fully ensure that the gas reaches every corner of the electrode uniformly, and improves the utilization rate of the reaction gas. Since the oxidant gas must pass through the boss of the serpentine channel from the inlet hole to reach the outlet hole on the diagonal side, this gas flow mode is conducive to the discharge of product water on the cathode side of the fuel cell. Metals such as Ag and Au are plated on the raised surfaces of the positive and negative plates, which can effectively improve the anti-corrosion, electrical conductivity or exhaust performance of the two plates. The metal frame 1 can be made of Al, stainless steel and other metals. The role of the metal frame can support and fix the strip-shaped groove part, which improves the shortcoming of the poor mechanical strength of the thin stainless steel plate, can realize the smooth installation of the fuel cell stack, and can form easy-to-process air passages and coolant passages . The present invention will give full play to the following functions of the bipolar plate: 1. The air channel can ensure the uniform distribution of fuel gas and oxidant gas; 2. The boss of the strip groove can ensure the uniform distribution of current and reduce the contact resistance to the greatest extent ; 3. The water cooling function can ensure the uniform distribution of the stack temperature; 4. The bipolar plate is composed of a strip groove part and a metal frame, which can not only make it have multiple functions but also have sufficient mechanical strength.

图1为本发明阳极板原理结构图。Fig. 1 is a schematic structural diagram of the anode plate of the present invention.

图2为本发明阴极板原理结构图。Fig. 2 is a schematic structural diagram of the cathode plate of the present invention.

图3为本发明图2中A-A剖视图。Fig. 3 is a sectional view of A-A in Fig. 2 of the present invention.

实施例1:Example 1:

采用0.15~0.5mm厚的奥氏体不锈钢冲压条状沟槽部分,其几何形状为矩形。根据电池的工作电流来确定矩形的边长,电流越大,面积越大。采用电焊的办法将完全对称的两块条状沟槽部分焊合在一起,其厚度根据需要可为1.5~3.5mm,结构如图1所示。冲压条状沟槽结构也如图1所示。其结构特点是凸台部分的始端和末端位于矩形短边的一侧,即冷却剂通道的始端和末端位于矩形短边的一侧,结构如图1所示。凸台部分的宽度2.0~6.0mm,沟槽部分的宽度0.5~3.0mm。呈蛇行条状沟槽的凸台与扩散层接触的部分局部电镀或化学镀Ag和Au的多层镀层,Ag层为底层表层为Au,银层的厚度以无孔为标准约5~10μm,金镀层0.1~05μm。另一部分是矩形的金属边框如图1所示。它可以用Al,Ti,Mg及其合金冲压或浇铸成型。结构特点是气体和液体通道都设在矩形的短边上。矩形的金属边框和条状沟槽部分通过粘合或焊接形成一体。Austenitic stainless steel with a thickness of 0.15 to 0.5 mm is used to stamp the strip-shaped groove part, and its geometric shape is rectangular. The side length of the rectangle is determined according to the working current of the battery. The larger the current, the larger the area. The method of electric welding is used to weld the two completely symmetrical strip groove parts together, and its thickness can be 1.5-3.5mm according to the needs. The structure is shown in Figure 1. The stamped strip groove structure is also shown in FIG. 1 . Its structural feature is that the start and end of the boss part are located on one side of the short side of the rectangle, that is, the start and end of the coolant channel are located on one side of the short side of the rectangle. The structure is shown in Figure 1. The width of the boss part is 2.0-6.0 mm, and the width of the groove part is 0.5-3.0 mm. Part of the part where the boss of the serpentine groove is in contact with the diffusion layer is partially electroplated or electroless plated with multi-layer plating of Ag and Au. The Ag layer is the bottom layer and the surface layer is Au. The thickness of the silver layer is about 5-10 μm based on the standard of no holes. The gold plating layer is 0.1-05 μm. The other part is a rectangular metal frame as shown in Figure 1. It can be stamped or cast with Al, Ti, Mg and their alloys. The structural feature is that the gas and liquid passages are located on the short sides of the rectangle. The rectangular metal frame and the strip groove part are formed into one by bonding or welding.

实施例2:Example 2:

采用0.15~0.5mm厚的Al,Ti及其合金冲压条状沟槽部分。其几何形状为矩形,根据电池的工作电流为确定矩形的边长,电流越大,面积越大。采用电焊的办法将完全对称的两块条状沟槽部分焊合在一起,其厚度根据需要可为1.5~3.5mm,结构如图1所示。冲压条状沟槽部分的结构如图1所示。其结构特点是凸台部分的始端和末端位于矩形短边的一侧,即冷却剂通道的始端和末端位于矩形短边的一侧,结构如图1所示。凸台部分的宽度2.0~6.0mm,沟槽部分的宽度0.5~3.0mm。呈蛇行条状沟槽的凸台与扩散层接触的部分局部电镀或化学镀Ag和Au的多层镀层。Ag层为底层表层为Au,银层的厚度以无孔为标准约5~10μm,金镀层0.1~05μm。另一部分是矩形的金属边框,如图1所示。它可以用Al,Ti,Mg及其合金冲压或浇铸成型。结构特点是气体和液体通道都设在矩形的短边上,矩形的金属边框和条状沟槽部分通过粘合或焊接形成一体。Al, Ti and their alloys with a thickness of 0.15-0.5 mm are used to stamp the strip-shaped groove part. Its geometric shape is a rectangle, and the side length of the rectangle is determined according to the working current of the battery. The larger the current, the larger the area. The method of electric welding is used to weld the two completely symmetrical strip groove parts together, and its thickness can be 1.5-3.5mm according to the needs. The structure is shown in Figure 1. The structure of the stamped strip groove part is shown in Figure 1. Its structural feature is that the start and end of the boss part are located on one side of the short side of the rectangle, that is, the start and end of the coolant channel are located on one side of the short side of the rectangle. The structure is shown in Figure 1. The width of the boss part is 2.0-6.0 mm, and the width of the groove part is 0.5-3.0 mm. Part of the part where the boss of the serpentine groove is in contact with the diffusion layer is partially electroplated or chemically plated with multilayer plating of Ag and Au. The Ag layer is the bottom layer and the surface layer is Au, the thickness of the silver layer is about 5-10 μm based on the standard of non-porous, and the gold plating layer is 0.1-05 μm. The other part is a rectangular metal frame, as shown in Figure 1. It can be stamped or cast with Al, Ti, Mg and their alloys. The structural feature is that the gas and liquid passages are arranged on the short side of the rectangle, and the rectangular metal frame and the strip groove part are formed into one by bonding or welding.

Claims (1)

1. the metal compound bipolar plate of a proton exchanging film fuel battery, it is characterized in that: in the middle of the metal edge frame [1], stud with two block structures, shape is the metal sheet [2] of symmetry fully, last metal sheet is a positive plate, following metal sheet is a minus plate, positive plate and minus plate are welded into an integral body, [1] two inferior horn place is drilled with circular hole [3] at metal edge frame, [4], the place, angle is drilled with square hole [7] respectively on metal edge frame [1] two, [8] and circular hole [5], [6], in circular hole [4], [6] locate machined grooves and snake type strip-shaped grooves and constitute gas passage, square hole [7], [8] locating to process groove links to each other with snake type coolant channel between two-plate, on positive plate through punching press, make the strip-shaped grooves boss that is the snake type, constituted the coolant channel of a snake type in the boss inside that is snake type strip-shaped grooves.
CN01132483A 2001-11-01 2001-11-01 Metal compound bipolar plate of fuel cell with proton exchange film Pending CN1416184A (en)

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Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100392895C (en) * 2006-07-27 2008-06-04 上海交通大学 Combined Monolithic Bipolar Plates for Proton Exchange Membrane Fuel Cells
CN100395911C (en) * 2006-06-13 2008-06-18 南京大学 fuel cell plate
CN100440595C (en) * 2007-01-05 2008-12-03 天津大学 Thin Metal Bipolar Plates for Proton Exchange Membrane Fuel Cells
CN100466351C (en) * 2007-08-02 2009-03-04 上海交通大学 Bipolar plates for proton exchange membrane fuel cells based on sheet stamping
CN100585927C (en) * 2005-05-13 2010-01-27 松下电器产业株式会社 The fuel cell
CN100588015C (en) * 2007-04-18 2010-02-03 新源动力股份有限公司 Sheet metal stamping forming metal bipolar plate
CN101094744B (en) * 2004-05-11 2010-04-21 通用汽车公司 Laser Welding of Metallic Bipolar Plates with Conductive Coating
CN101950807A (en) * 2009-07-10 2011-01-19 通用汽车环球科技运作公司 Low cost manganese stabilisation austenitic stainless steel alloy, comprise the bipolar plates of this alloy and comprise the fuel cell system of this bipolar plates
CN101281969B (en) * 2003-05-12 2011-03-30 三菱综合材料株式会社 Composite porous body, gas diffusion layer member, cell member, and manufacturing method thereof
CN102299357A (en) * 2011-08-10 2011-12-28 清华大学 Composite electrode plate for electrochemical reactor and manufacturing method thereof
WO2013029514A1 (en) * 2011-09-01 2013-03-07 上海恒劲动力科技有限公司 Fuel cell with integrated cathode-anode bipolar plate
CN105762367A (en) * 2014-12-16 2016-07-13 中国科学院大连化学物理研究所 Fuel cell bipolar plate
CN108063264A (en) * 2017-12-18 2018-05-22 中国科学院青岛生物能源与过程研究所 A kind of graphite-metal frame composite dual-electrode plates and preparation method thereof
CN112086659A (en) * 2020-08-25 2020-12-15 北京理工大学 Fuel cell stack convenient for temperature control

Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101281969B (en) * 2003-05-12 2011-03-30 三菱综合材料株式会社 Composite porous body, gas diffusion layer member, cell member, and manufacturing method thereof
CN101094744B (en) * 2004-05-11 2010-04-21 通用汽车公司 Laser Welding of Metallic Bipolar Plates with Conductive Coating
CN100585927C (en) * 2005-05-13 2010-01-27 松下电器产业株式会社 The fuel cell
CN100395911C (en) * 2006-06-13 2008-06-18 南京大学 fuel cell plate
CN100392895C (en) * 2006-07-27 2008-06-04 上海交通大学 Combined Monolithic Bipolar Plates for Proton Exchange Membrane Fuel Cells
CN100440595C (en) * 2007-01-05 2008-12-03 天津大学 Thin Metal Bipolar Plates for Proton Exchange Membrane Fuel Cells
CN100588015C (en) * 2007-04-18 2010-02-03 新源动力股份有限公司 Sheet metal stamping forming metal bipolar plate
CN100466351C (en) * 2007-08-02 2009-03-04 上海交通大学 Bipolar plates for proton exchange membrane fuel cells based on sheet stamping
CN101950807A (en) * 2009-07-10 2011-01-19 通用汽车环球科技运作公司 Low cost manganese stabilisation austenitic stainless steel alloy, comprise the bipolar plates of this alloy and comprise the fuel cell system of this bipolar plates
CN102299357A (en) * 2011-08-10 2011-12-28 清华大学 Composite electrode plate for electrochemical reactor and manufacturing method thereof
CN102299357B (en) * 2011-08-10 2013-07-10 清华大学 Composite electrode plate for electrochemical reactor and manufacturing method thereof
WO2013029514A1 (en) * 2011-09-01 2013-03-07 上海恒劲动力科技有限公司 Fuel cell with integrated cathode-anode bipolar plate
CN105762367A (en) * 2014-12-16 2016-07-13 中国科学院大连化学物理研究所 Fuel cell bipolar plate
CN105762367B (en) * 2014-12-16 2018-04-24 中国科学院大连化学物理研究所 A kind of fuel battery double plates
CN108063264A (en) * 2017-12-18 2018-05-22 中国科学院青岛生物能源与过程研究所 A kind of graphite-metal frame composite dual-electrode plates and preparation method thereof
CN112086659A (en) * 2020-08-25 2020-12-15 北京理工大学 Fuel cell stack convenient for temperature control

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