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CN106887633B - High-temperature fuel cell stack - Google Patents

High-temperature fuel cell stack Download PDF

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CN106887633B
CN106887633B CN201510932806.9A CN201510932806A CN106887633B CN 106887633 B CN106887633 B CN 106887633B CN 201510932806 A CN201510932806 A CN 201510932806A CN 106887633 B CN106887633 B CN 106887633B
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fuel cell
molecular sieve
water
high temperature
cell stack
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CN106887633A (en
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孙公权
孙雪敬
杨林林
孙海
戚甫来
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Dalian Institute of Chemical Physics of CAS
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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
    • H01M8/24Grouping of fuel cells, e.g. stacking of fuel cells
    • H01M8/2465Details of groupings of fuel cells
    • H01M8/247Arrangements for tightening a stack, for accommodation of a stack in a tank or for assembling different tanks
    • 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
    • H01M8/0204Non-porous and characterised by the material
    • H01M8/0223Composites
    • H01M8/0228Composites in the form of layered or coated products
    • 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
    • H01M8/04291Arrangements for managing water in solid electrolyte fuel cell systems
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/10Fuel cells with solid electrolytes
    • H01M8/12Fuel cells with solid electrolytes operating at high temperature, e.g. with stabilised ZrO2 electrolyte
    • 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)
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  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Fuel Cell (AREA)
  • Composite Materials (AREA)

Abstract

一种高温燃料电池电堆,包括二个端板和置于二个端板间的单体电池,所述单体电池包括双极板和膜电极,于所述端板靠近单体电池的内侧表面和/或所述双极板两侧表面涂覆有分子筛涂层。根据本发明设计,可以有效解决高温质子交换膜燃料电池启停过程中由于水不能及时排出而导致的电池性能下降的问题。提高了电池运行过程中的稳定性,使电池寿命得以提升。解决了电池运行过程中由于生成的水不能及时排除而导致的水淹现象,使膜电极中催化剂载体和贵金属催化剂以及扩散层等材料的腐蚀得以减轻,使膜电极稳定性得到提高。本发明所述除水方法结构简单,能够在不加外部设施的条件下进行有效除水。A high-temperature fuel cell stack, comprising two end plates and a single cell placed between the two end plates, the single cell comprising a bipolar plate and a membrane electrode, and the end plate is close to the inner side of the single cell The surface and/or both sides of the bipolar plate are coated with a molecular sieve coating. According to the design of the present invention, the problem that the performance of the high temperature proton exchange membrane fuel cell is degraded due to the inability to discharge water in time during the start and stop of the high temperature proton exchange membrane fuel cell can be effectively solved. Improve the stability of the battery during operation, so that the battery life can be improved. The water flooding phenomenon caused by the fact that the generated water cannot be removed in time during the operation of the battery is solved, the corrosion of the catalyst carrier, the noble metal catalyst, the diffusion layer and other materials in the membrane electrode is reduced, and the stability of the membrane electrode is improved. The water removal method of the invention has a simple structure and can effectively remove water without adding external facilities.

Description

一种高温燃料电池电堆A high temperature fuel cell stack

技术领域technical field

本发明涉及燃料电池技术领域,具体的说涉及一种高温燃料电池电堆。The invention relates to the technical field of fuel cells, in particular to a high temperature fuel cell stack.

背景技术Background technique

燃料电池是一种通过化学反应将储存在化合物燃料中的化学能直接转化为电能的装置。质子交换膜燃料电池通常由阳极、阴极及质子交换膜组成。在电池运行过程中,燃料在阳极催化剂表面发生氧化反应生成质子和电子,质子通过质子交换膜到达阴极,氧气在阴极催化剂表面与质子发生还原反应生成水,电子则通过外电路做功到达阴极。A fuel cell is a device that directly converts chemical energy stored in compound fuels into electrical energy through chemical reactions. A proton exchange membrane fuel cell usually consists of an anode, a cathode and a proton exchange membrane. During the operation of the battery, the fuel undergoes oxidation reaction on the surface of the anode catalyst to generate protons and electrons, the protons reach the cathode through the proton exchange membrane, oxygen undergoes a reduction reaction with protons on the surface of the cathode catalyst to generate water, and the electrons work through the external circuit to reach the cathode.

质子交换膜燃料电池放电过程会产生大量的水,高温质子交换膜燃料电池由于运行温度较高,水以气态形式伴随阴极尾气一同排入大气,但在电池启停过程中温度较低,液态水不足以汽化致使电池产生的水不能及时排出导致电池性能下降。A large amount of water is generated during the discharge process of the PEM fuel cell. Due to the high operating temperature of the high temperature PEM fuel cell, the water is discharged into the atmosphere in a gaseous form along with the cathode exhaust gas, but the temperature is low during the start and stop process of the cell, and the liquid water is insufficient. Due to vaporization, the water produced by the battery cannot be discharged in time, resulting in a decrease in battery performance.

发明内容SUMMARY OF THE INVENTION

本发明目的是为了解决高温质子交换膜燃料电池系统在启停过程中生成的水难以排出而导致水淹的问题,提出了一种有效除水方法。The purpose of the present invention is to provide an effective water removal method in order to solve the problem that the water generated during the startup and shutdown of the high temperature proton exchange membrane fuel cell system is difficult to discharge and causes flooding.

本发明采用以下具体方式来实现:The present invention adopts the following concrete ways to realize:

一种高温燃料电池电堆,包括二个端板和置于二个端板间的单体电池,所述单体电池包括双极板和膜电极,于所述端板靠近单体电池的内侧表面和/或所述双极板两侧表面涂覆有分子筛涂层。A high-temperature fuel cell stack, comprising two end plates and a single cell placed between the two end plates, the single cell comprising a bipolar plate and a membrane electrode, and the end plate is close to the inner side of the single cell The surface and/or both sides of the bipolar plate are coated with a molecular sieve coating.

于所述电堆阴极出口管路内表面涂覆有分子筛涂层。A molecular sieve coating is coated on the inner surface of the stack cathode outlet pipeline.

于所述端板靠近单体电池的内侧流道表面和/或所述双极板两侧流道表面涂覆有分子筛涂层。Molecular sieve coating is applied on the surface of the inner flow channel of the end plate close to the single cell and/or the surface of the flow channel on both sides of the bipolar plate.

所述分子筛为低温吸水且高温脱水材料。The molecular sieve is a low-temperature water-absorbing and high-temperature dehydrating material.

所述分子筛为3A、4A、5A、10X、13X中的一种或两种以上的混合物。The molecular sieve is one or a mixture of two or more of 3A, 4A, 5A, 10X, and 13X.

所述分子筛涂层为分子筛膜。The molecular sieve coating is a molecular sieve membrane.

所述分子筛涂层的厚度为0.001-10mm。The thickness of the molecular sieve coating is 0.001-10 mm.

根据本发明设计,可以有效解决高温质子交换膜燃料电池启停过程中由于水不能及时排出而导致的电池性能下降的问题。提高了电池运行过程中的稳定性,使电池寿命得以提升。解决了电池运行过程中由于生成的水不能及时排除而导致的水淹现象,使膜电极中催化剂载体和贵金属催化剂以及扩散层等材料的腐蚀得以减轻,使膜电极稳定性得到提高。本发明所述除水方法结构简单,能够在不加外部设施的条件下进行有效除水。According to the design of the present invention, the problem that the performance of the high temperature proton exchange membrane fuel cell is degraded due to the inability to discharge water in time during the start and stop of the high temperature proton exchange membrane fuel cell can be effectively solved. Improve the stability of the battery during operation, so that the battery life can be improved. The water flooding phenomenon caused by the fact that the generated water cannot be removed in time during the operation of the battery is solved, the corrosion of the catalyst carrier, the noble metal catalyst, the diffusion layer and other materials in the membrane electrode is reduced, and the stability of the membrane electrode is improved. The water removal method of the invention has a simple structure and can effectively remove water without adding external facilities.

附图说明Description of drawings

图1为双极板流道分布及分子筛涂层分布图;Fig. 1 is bipolar plate flow channel distribution and molecular sieve coating distribution diagram;

1、端板;2、分子筛涂层;3、阳极催化层;4、质子交换膜;5、阴极催化层;6、双极板1. End plate; 2. Molecular sieve coating; 3. Anode catalytic layer; 4. Proton exchange membrane; 5. Cathode catalytic layer; 6. Bipolar plate

图2为高温燃料电池电堆装配图;Figure 2 is an assembly diagram of a high temperature fuel cell stack;

图3为膜电极装配MEA图。Figure 3 is a diagram of the membrane electrode assembly MEA.

具体实施方式Detailed ways

下面参照附图等来说明本发明的具体实施方式。Specific embodiments of the present invention will be described below with reference to the accompanying drawings and the like.

具体实施方式包括:Specific implementations include:

端板1,用于流体分配与集流;分子筛涂层2,在电池启停过程中除水;阳极催化层3,催化燃料的氧化反应;质子交换膜4,传输质子,隔绝阴阳极反应物;阴极催化层5,催化氧气的还原反应;双极板6,阴阳极反应物的流体分配。工作原理:End plate 1, used for fluid distribution and current collection; Molecular sieve coating 2, water removal during battery start-up and shutdown; Anode catalytic layer 3, catalyzed fuel oxidation reaction; Proton exchange membrane 4, Proton transmission, isolation of cathode and anode reactants ; Cathode catalytic layer 5, catalyzes the reduction reaction of oxygen; Bipolar plate 6, fluid distribution of cathode and anode reactants. working principle:

分子筛涂层2涂覆于端板1和双极板6的流道上,阳极催化层3、质子交换膜4与阴极催化层5共同组成膜电极装配MEA,MEA组装与端板与双极板以及双极板之间。The molecular sieve coating 2 is coated on the flow channel of the end plate 1 and the bipolar plate 6. The anode catalytic layer 3, the proton exchange membrane 4 and the cathode catalytic layer 5 together form the membrane electrode assembly MEA, which is assembled with the end plate and the bipolar plate and between the bipolar plates.

高温质子交换膜燃料电池使用的是PBI膜,其质子传输不依靠水的作用,因而其可在相对湿度较低的情况下使用,本实施方法将分子筛涂覆到端板与双极板的流道内以及在电池尾排口进行分子筛的涂覆从而达到启停过程除水的目的。该分子筛须具有以下功能:在温度较低时(低于120℃)具有吸附水的作用,在温度较高时(高于150℃)能够将低温时吸附的水进行脱附。The high temperature proton exchange membrane fuel cell uses a PBI membrane, and its proton transport does not rely on the action of water, so it can be used in the case of low relative humidity. Molecular sieve coating is carried out in the channel and at the tail discharge port of the battery to achieve the purpose of removing water during the start-stop process. The molecular sieve must have the following functions: when the temperature is low (below 120°C), it can adsorb water, and when the temperature is high (higher than 150°C), it can desorb the water adsorbed at low temperature.

在高温燃料电池电堆启停过程中,由于温度较低,电池放电产生的水不能以气态的形式及时排出而滞留在电池内部,导致高温燃料电池电堆发生水淹从而使高温燃料电池电堆性能衰减。若在流道上涂覆具有吸水性能的分子筛涂层,通过流道上涂覆的吸水分子筛将放电过程中产生的水吸附在分子筛内部,可有效避免水淹现象的发生。当高温燃料电池电堆运行到正常运行温度时,此时生成的水以气态形式随同尾气一同排出。由于高温燃料电池电堆正常运行温度较高,因而可使分子筛将低温时吸附的水脱附出去,变为气态水随同尾气一同排出。During the start-stop process of the high-temperature fuel cell stack, due to the low temperature, the water generated by the discharge of the battery cannot be discharged in a gaseous form in time and stays inside the battery, resulting in flooding of the high-temperature fuel cell stack and causing the high-temperature fuel cell stack to flood. performance degradation. If a molecular sieve coating with water-absorbing properties is coated on the flow channel, the water generated during the discharge process is adsorbed inside the molecular sieve by the water-absorbing molecular sieve coated on the flow channel, which can effectively avoid the occurrence of flooding. When the high temperature fuel cell stack operates to the normal operating temperature, the water generated at this time is discharged together with the exhaust gas in the form of gas. Due to the high normal operating temperature of the high-temperature fuel cell stack, the molecular sieve can desorb the water adsorbed at low temperature, and turn it into gaseous water and discharge it together with the exhaust gas.

实施方式一:该实施方式将20节单池置于两个端板之间组成高温燃料电池电堆,于端板靠近单体电池的内侧表面和双极板两侧表面涂覆有3A分子筛涂层,该分子筛膜的厚度为0.005mm。Embodiment 1: In this embodiment, 20 single cells are placed between two end plates to form a high-temperature fuel cell stack. layer, the thickness of the molecular sieve membrane is 0.005mm.

通过该方式组装的高温燃料电池电堆在持续启停100次后未发现明显的电池性能的下降,而为涂覆该分子筛膜的高温燃料电池电堆在与上述高温燃料电池电堆在相同条件下启停73次之后出现明显的由于水淹而导致的电池性能的下降。通过两种方式的对比发现,上述方式可有效改善高温燃料电池电堆在启停过程中导致的水淹现象。The high temperature fuel cell stack assembled in this way did not find obvious decrease in cell performance after 100 times of continuous start and stop, but the high temperature fuel cell stack coated with the molecular sieve membrane was under the same conditions as the above high temperature fuel cell stack. After starting and stopping 73 times, the battery performance decreased obviously due to flooding. Through the comparison of the two methods, it is found that the above method can effectively improve the flooding phenomenon caused by the high temperature fuel cell stack during the start-stop process.

实施方式二:该实施方式将20节单池置于两个端板之间组成高温燃料电池电堆,于端板靠近单体电池的内侧表面和双极板两侧表面涂覆有5A分子筛涂层,该分子筛膜的厚度为0.01mm。Embodiment 2: In this embodiment, 20 single cells are placed between two end plates to form a high-temperature fuel cell stack. layer, the thickness of the molecular sieve membrane is 0.01mm.

通过该方式组装的高温燃料电池电堆在持续启停100次后未发现明显的电池性能的下降,而为涂覆该分子筛膜的高温燃料电池电堆在与上述高温燃料电池电堆在相同条件下启停73次之后出现明显的由于水淹而导致的电池性能的下降。通过两种方式的对比发现,上述方式可有效改善高温燃料电池电堆在启停过程中导致的水淹现象。The high temperature fuel cell stack assembled in this way did not find obvious decrease in cell performance after 100 times of continuous start and stop, but the high temperature fuel cell stack coated with the molecular sieve membrane was under the same conditions as the above high temperature fuel cell stack. After starting and stopping 73 times, the battery performance decreased obviously due to flooding. Through the comparison of the two methods, it is found that the above method can effectively improve the flooding phenomenon caused by the high temperature fuel cell stack during the start-stop process.

本实施方式所述燃料电池除湿系统可以在高温燃料电池电堆启停阶段将电池内生成的水进行有效吸附,避免了水淹现象的发生。在高温燃料电池电堆温度较高时,分子筛内吸附的水可进行脱附,从而保证了分子筛的循环使用,使分子筛在流道内进行涂覆的方法得以实现。该系统还在电池的尾排口处涂覆有该分子筛,其主要作用是保证电池在非运行状态时的干燥。由于各地空气在不同季节具有不同的湿度,高温燃料电池电堆在非运行状态时其尾排口始终与大气保持连通状态,这也意味着空气中的水可随同空气进入电池内部,严重时会导致电池内部一些器件的腐蚀。在尾排口处放置吸水分子筛主要是为了吸附空气中含有的水,避免空气中的水进入电池内部对电池进行腐蚀。The fuel cell dehumidification system described in this embodiment can effectively adsorb the water generated in the cell during the start and stop phases of the high temperature fuel cell stack, thereby avoiding the occurrence of flooding. When the temperature of the high-temperature fuel cell stack is high, the water adsorbed in the molecular sieve can be desorbed, thereby ensuring the recycling of the molecular sieve and realizing the method of coating the molecular sieve in the flow channel. The system is also coated with the molecular sieve at the tail discharge port of the battery, the main function of which is to ensure the drying of the battery in the non-operating state. Since the air in different places has different humidity in different seasons, the tail exhaust port of the high-temperature fuel cell stack is always in communication with the atmosphere when it is not in operation, which also means that the water in the air can enter the interior of the battery with the air. Causes corrosion of some devices inside the battery. The purpose of placing the water-absorbing molecular sieve at the tail discharge port is to absorb the water contained in the air and prevent the water in the air from entering the battery and corroding the battery.

Claims (4)

1.一种高温质子交换膜燃料电池电堆,包括两个端板和置于两个端板间的单体电池,所述单体电池包括2个以上由双极板间隔的膜电极MEA,其特征在于:于所述端板靠近单体电池的内侧流道表面、所述双极板两侧流道表面以及所述电堆阴极出口管路内表面涂覆有分子筛涂层;1. A high temperature proton exchange membrane fuel cell stack, comprising two end plates and a single cell placed between the two end plates, the single cell comprising more than 2 membrane electrode MEAs separated by bipolar plates, It is characterized in that: the surface of the inner flow channel of the end plate close to the single cell, the surface of the flow channel on both sides of the bipolar plate and the inner surface of the stack cathode outlet pipeline are coated with molecular sieve coating; 所述分子筛为低于120℃的低温时吸水且高于150℃的高温时脱水的材料。The molecular sieve is a material that absorbs water at a low temperature lower than 120°C and dehydrates at a high temperature higher than 150°C. 2.如权利要求1所述高温质子交换膜燃料电池电堆,其特征在于:所述分子筛为3A、4A、5A、10X、13X中的一种或两种以上的混合物。2 . The high temperature proton exchange membrane fuel cell stack of claim 1 , wherein the molecular sieve is one or a mixture of two or more of 3A, 4A, 5A, 10X, and 13X. 3 . 3.如权利要求1所述高温质子交换膜燃料电池电堆,其特征在于:所述分子筛涂层为分子筛膜。3 . The high temperature proton exchange membrane fuel cell stack of claim 1 , wherein the molecular sieve coating is a molecular sieve membrane. 4 . 4.如权利要求1所述高温质子交换膜燃料电池电堆,其特征在于:所述分子筛涂层的厚度为0.001-10mm。4 . The high temperature proton exchange membrane fuel cell stack of claim 1 , wherein the molecular sieve coating has a thickness of 0.001-10 mm. 5 .
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