CN109888325B - Multi-stage uniform flow field fuel cell and working method thereof - Google Patents
Multi-stage uniform flow field fuel cell and working method thereof Download PDFInfo
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Abstract
本发明公开一种多级均匀流场燃料电池及其工作方法,本发明的多级均匀流场燃料电池,树状燃料供给支路通过逐级分散的树状流场由燃料分配流路展开,采用树状逐级分散的纵向流入流场,保证电解液能够均匀的进入电极表面,提高电解液反应程度,进一步提升电池效率;同时,阵列状产物排出支路均匀分布连接在产物回收流路上,采用与流入流场相结合的阵列分布纵向流出流场,保证电解液在反应完成后能够顺流流出电极,保证电极侧燃料始终均匀高浓度,避免了燃料与产物的掺混。
The invention discloses a multi-level uniform flow field fuel cell and a working method thereof. In the multi-level uniform flow field fuel cell of the present invention, a tree-shaped fuel supply branch is expanded from a fuel distribution flow path through a tree-shaped flow field dispersed step by step, The vertical inflow flow field with dendritic dispersion is adopted to ensure that the electrolyte can enter the electrode surface evenly, improve the reaction degree of the electrolyte, and further improve the battery efficiency. The vertical outflow flow field is distributed in an array combined with the inflow flow field to ensure that the electrolyte can flow out of the electrode downstream after the reaction is completed, to ensure that the fuel on the electrode side is always at a uniform and high concentration, and to avoid the mixing of fuel and products.
Description
技术领域technical field
本发明涉及燃料电池技术领域,具体涉及一种多级均匀流场燃料电池。The invention relates to the technical field of fuel cells, in particular to a multi-level uniform flow field fuel cell.
背景技术Background technique
能源是人类赖以生存和发展的重要物质基础,人类社会的一切活动都离不开能源。随着经济的高速发展和社会的不断进步,人类对能源的消耗量也持续增长。世界范围内能源需求持续增长,传统化石能源消耗量仍占主导。然而,传统化石能源储量有限,部分能源在未来几十年将消耗殆尽。此外,在传统化石能源利用过程中,环境污染问题也在日益加剧,由此带来的“温室效应”、“酸雨”、“臭氧层破坏”等问题严重威胁着人类的生存和发展。面对着能源危机和环境保护的严峻挑战,寻找能够替代传统化石能源的清洁可持续能源成为当然人类研究的重点。Energy is an important material basis for human survival and development, and all activities of human society are inseparable from energy. With the rapid development of the economy and the continuous progress of the society, the consumption of energy by human beings also continues to increase. Global energy demand continues to grow, and traditional fossil energy consumption still dominates. However, traditional fossil energy reserves are limited, some of which will be exhausted in the coming decades. In addition, in the process of traditional fossil energy utilization, the problem of environmental pollution is also increasing day by day, and the resulting problems such as "greenhouse effect", "acid rain" and "destruction of the ozone layer" seriously threaten the survival and development of human beings. Faced with the severe challenges of energy crisis and environmental protection, finding clean and sustainable energy that can replace traditional fossil energy has become the focus of human research.
目前,太阳能、风能、潮汐能、地热能等具有能源充足,利用过程清洁无污染等优点。但是这类能源在利用过程中存在间歇性、不稳定性、效率低等问题。燃料电池由于其能量转换效率高、污染小、无噪音等优点而受到人们的广泛关注。作为新一代能源技术,燃料电池为解决能源危机和环境污染问题提供了一种新思路,具有战略性意义。燃料电池技术是一种新型发电技术,该技术可以将存在于燃料与氧化剂中的化学能直接转化为电能,具有高效、无污染、无噪声、可靠性高、模块化、对负载变化可以快速响应等显著优点,被认为是解决能源危机的终极方案。At present, solar energy, wind energy, tidal energy, geothermal energy, etc. have the advantages of sufficient energy, clean and pollution-free utilization process. However, there are some problems such as intermittency, instability and low efficiency in the utilization process of this kind of energy. Fuel cells have attracted extensive attention due to their high energy conversion efficiency, low pollution, and no noise. As a new generation of energy technology, fuel cells provide a new way of thinking for solving energy crisis and environmental pollution problems, which is of strategic significance. Fuel cell technology is a new type of power generation technology, which can directly convert chemical energy in fuel and oxidant into electrical energy, with high efficiency, no pollution, no noise, high reliability, modularity, and fast response to load changes. It is considered to be the ultimate solution to the energy crisis.
燃料电池主要由离子交换膜、阴阳电极和双极板构成。其中由阴极电极、离子交换膜和阳极电极构成的膜电极(membrane electrode assembly,MEA)是燃料电池发生电化学反应的场所。燃料和氧化剂分别通入电池的阳极和阴极。通入阳极的燃料(如H2、CH3OH、CH3CH2OH、CO(NH2)2、NaBH4、HCOONa等)发生氧化反应释放出电子,电子通过外电路流入到阴极,并与阴极的氧化剂(如O2、H2O2等)结合发生还原反应。同时离子通过电解质膜迁移到阴极(或阳极),构成回路。The fuel cell is mainly composed of ion exchange membrane, cathode and anode electrodes and bipolar plates. The membrane electrode (MEA), which is composed of a cathode electrode, an ion exchange membrane and an anode electrode, is the place where the electrochemical reaction of the fuel cell occurs. Fuel and oxidant are passed to the anode and cathode of the cell, respectively. The fuel (such as H 2 , CH 3 OH, CH 3 CH 2 OH, CO(NH 2 ) 2 , NaBH 4 , HCOONa, etc.) fed into the anode undergoes an oxidation reaction to release electrons, and the electrons flow into the cathode through the external circuit and interact with the anode. The oxidant (such as O 2 , H 2 O 2 , etc.) of the cathode combines and undergoes a reduction reaction. At the same time, ions migrate through the electrolyte membrane to the cathode (or anode), forming a circuit.
在众多类型的燃料电池中,直接液体燃料电池(Direct liquid fuel cells,DLFC)由于燃料能量密度高、便于储存和运输等优点,近些年来受到人们的广泛关注。直接液体燃料电池是以甲醇、乙醇、尿素、硼氢化钠、甲酸盐等液体作为燃料的一类燃料电池。按照固体电解质膜种类的不同,直接液体燃料电池可分为酸性直接液体燃料电池和碱性直接液体燃料电池。Among many types of fuel cells, direct liquid fuel cells (DLFC) have received extensive attention in recent years due to the advantages of high fuel energy density, convenient storage and transportation, etc. Direct liquid fuel cells use methanol, ethanol, urea, sodium borohydride, formate and other liquids as fuels. According to the different types of solid electrolyte membranes, direct liquid fuel cells can be divided into acidic direct liquid fuel cells and alkaline direct liquid fuel cells.
作为直接液体燃料电池的关键部位,阳极流场起到了输送燃料、分配燃料、回收产物的功能,在整个燃料电池运行过程中起着很关键的作用。当前燃料电池阳极流场主要包括蛇形流场、平行流场、非连续型流场、交指型流场等,其主要通过燃料在电极一侧流动时的扩散作用进入电极反应。在这一过程中,随着燃料在流道中的流动及在电极中的扩散反应,燃料不断消耗产物不断进入流道中,燃料的浓度逐渐降低,这导致电极内燃料浓度分布不均匀,降低了电极反应效率,进一步降低了直接液体燃料电池的工作效率。As a key part of the direct liquid fuel cell, the anode flow field plays the functions of transporting fuel, distributing fuel, and recovering products, and plays a key role in the entire fuel cell operation process. The current fuel cell anode flow field mainly includes serpentine flow field, parallel flow field, discontinuous flow field, interdigitated flow field, etc., which mainly enter the electrode reaction through the diffusion of fuel flowing on one side of the electrode. In this process, with the flow of fuel in the flow channel and the diffusion reaction in the electrode, the fuel is continuously consumed and the product continuously enters the flow channel, and the concentration of the fuel gradually decreases, which leads to the uneven distribution of the fuel concentration in the electrode and reduces the electrode. The reaction efficiency further reduces the working efficiency of the direct liquid fuel cell.
因此,针对燃料电池燃料在流动反应过程中出现的燃料产物掺混、燃料浓度分布不均匀等问题,一种燃料产物相分离顺流传递、燃料浓度均匀分布的高效燃料电池亟待出现。Therefore, in view of the problems of fuel product blending and uneven fuel concentration distribution in the fuel cell fuel flow reaction process, a high-efficiency fuel cell with phase-separated co-current transfer of fuel products and uniform fuel concentration distribution is urgently needed.
发明内容SUMMARY OF THE INVENTION
针对上述现有技术存在的问题,本发明目的在于提供一种多级均匀流场燃料电池及其工作方法,使燃料能够直接且均匀的到达电极表面,保证燃料与产物的顺流传输,避免燃料产物的掺混。In view of the problems existing in the above-mentioned prior art, the purpose of the present invention is to provide a multi-level uniform flow field fuel cell and a working method thereof, so that the fuel can reach the electrode surface directly and uniformly, ensure the co-current transmission of the fuel and the product, and avoid the fuel Blending of products.
为达到上述目的,本发明采用以下技术方案予以实现:To achieve the above object, the present invention adopts the following technical solutions to realize:
一种多级均匀流场燃料电池,包括设置在燃料电池本体上的阳极流场板、阳极集流板、阳极电极、交换膜、阴极电极、阴极集流板和阴极流场板;A multi-level uniform flow field fuel cell, comprising an anode flow field plate, an anode current collector plate, an anode electrode, an exchange membrane, a cathode electrode, a cathode current collector plate and a cathode flow field plate arranged on the fuel cell body;
阳极集流板与阳极流场板和阳极电极相连,阳极电极和阴极电极通过交换膜隔开,阴极集流板与阴极电极和阴极流场板相连;The anode current collector plate is connected with the anode flow field plate and the anode electrode, the anode electrode and the cathode electrode are separated by an exchange membrane, and the cathode current collector plate is connected with the cathode electrode and the cathode flow field plate;
阳极流场板为设置有燃料进口、燃料分配流路、树状燃料供给支路、阵列状产物排出支路、产物回收流路和产物出口的流场板,其中树状燃料供给支路通过逐级分散的树状流场由燃料分配流路展开,阵列状产物排出支路均匀分布连接在产物回收流路上;The anode flow field plate is a flow field plate provided with a fuel inlet, a fuel distribution flow path, a tree-shaped fuel supply branch, an array-shaped product discharge branch, a product recovery flow path, and a product outlet, wherein the tree-shaped fuel supply branch passes through one by one. The hierarchically dispersed tree-like flow field is expanded by the fuel distribution flow path, and the array-shaped product discharge branches are evenly distributed and connected to the product recovery flow path;
燃料进口为燃料分配流路与燃料电池外侧相连的进口,树状燃料供给支路进口与燃料分配流路相连,树状燃料供给支路出口通过阳极集流板与阳极电极相连,阵列状产物排出支路进口通过阳极集流板与阳极电极相连,阵列状产物排出支路出口与产物回收流路相连,树状燃料供给支路和阵列状产物排出支路为位于阳极流场板中互相交错不连通的管路,产物出口为产物回收流路与燃料电池外侧相连的出口;The fuel inlet is the inlet connecting the fuel distribution flow path to the outside of the fuel cell, the tree-shaped fuel supply branch inlet is connected to the fuel distribution flow path, the tree-shaped fuel supply branch outlet is connected to the anode electrode through the anode current collector, and the array-shaped products are discharged The inlet of the branch is connected to the anode electrode through the anode current collector plate, the outlet of the array-shaped product discharge branch is connected to the product recovery flow path, and the dendritic fuel supply branch and the array-shaped product discharge branch are located in the anode flow field plate in a staggered manner. The connected pipeline, the product outlet is the outlet connecting the product recovery flow path and the outside of the fuel cell;
阳极集流板为具有阵列分布孔的平板,阳极集流板中孔道与树状燃料供给支路出口及阵列状产物排出支路进口相连通,阴极集流板为与阴极流场板流道相对应的具有孔道的平板,阴极流场板为具有流道的平板。The anode current collector plate is a flat plate with an array of distribution holes, the holes in the anode current collector plate are connected with the outlet of the tree-shaped fuel supply branch and the inlet of the array-shaped product discharge branch, and the cathode current collector plate is in phase with the flow channel of the cathode flow field plate. Correspondingly, the flat plate with pores, and the cathode flow field plate is a flat plate with flow channels.
进一步,所述产物回收流路纵向设置在阳极流场板中,产物出口位于阳极流场板顶部,燃料进口位于阳极流场板侧壁上。Further, the product recovery flow path is longitudinally arranged in the anode flow field plate, the product outlet is located at the top of the anode flow field plate, and the fuel inlet is located on the side wall of the anode flow field plate.
进一步,多条所述树状燃料供给支路出口和多条阵列状产物排出支路进口等间距间隔设置。Further, a plurality of the tree-shaped fuel supply branch outlets and a plurality of array-shaped product discharge branch inlets are arranged at equal intervals.
进一步,所述树状燃料供给支路为二叉树状逐级分散流场,即树状燃料供给支路由1条电解液供给流路以90°旋转阵列分为4条支路,4条支路进一步分为16条支路,通过“1-4-16”逐级分散方式分布。Further, the dendritic fuel supply branch is a binary tree-like dispersed flow field step by step, that is, the dendritic fuel supply branch is divided into 4 branches by a 90° rotating array of one electrolyte supply flow path, and the 4 branches are further Divided into 16 branches, distributed through "1-4-16" step-by-step dispersion.
进一步,所述阵列状产物排出支路以“3×3”阵列分布于电极外侧。Further, the array-shaped product discharge branches are distributed outside the electrode in a "3×3" array.
进一步,所述阳极流场板和阴极流场板所用材料为无机非金属材料、金属复合材料或有机高分子材料。Further, the materials used for the anode flow field plate and the cathode flow field plate are inorganic non-metallic materials, metal composite materials or organic polymer materials.
进一步,所述阳极集流板和阴极集流板材料为无机非金属或金属的导电材料。Further, the materials of the anode current collector plate and the cathode current collector plate are inorganic non-metallic or metallic conductive materials.
进一步,所述阳极电极和阴极电极为涂覆有相应催化剂具有多孔结构的导电金属材料或碳材料。Further, the anode electrode and the cathode electrode are conductive metal materials or carbon materials coated with corresponding catalysts and having a porous structure.
进一步,所述交换膜为阳离子交换膜、阴离子交换膜或中性交换膜;Further, the exchange membrane is a cation exchange membrane, an anion exchange membrane or a neutral exchange membrane;
一种多级均匀流场燃料电池的工作方法,包括如下步骤:A working method of a multi-level uniform flow field fuel cell, comprising the following steps:
步骤S100:燃料均匀分配进入电极:Step S100: The fuel is evenly distributed into the electrodes:
燃料电池未反应的燃料通过燃料进口进入燃料电池阳极侧,在泵功的作用下通过燃料分配流路均匀分配到树状燃料供给支路,进入阳极电极中;同时,氧化剂通过阴极流场板和阴极集流板进入阴极电极中;The unreacted fuel of the fuel cell enters the anode side of the fuel cell through the fuel inlet, and is evenly distributed to the tree-like fuel supply branch through the fuel distribution flow path under the action of the pump power, and enters the anode electrode; at the same time, the oxidant passes through the cathode flow field plate and The cathode current collector plate enters the cathode electrode;
步骤S200:电池放电反应:Step S200: battery discharge reaction:
燃料在阳极电极表面进行放电反应;The fuel undergoes a discharge reaction on the surface of the anode electrode;
步骤S300:产物顺流流出电池:Step S300: The product flows out of the battery downstream:
燃料反应完成后,由每个树状燃料供给支路出口流入的燃料经过阳极电极由阵列状产物排出支路入口顺流流出,汇流至产物回收流路通过产物出口排出。After the fuel reaction is completed, the fuel flowing in from the outlet of each dendritic fuel supply branch passes through the anode electrode and flows out from the inlet of the array-shaped product discharge branch, and converges to the product recovery flow path and is discharged through the product outlet.
本发明相对于现有技术,具有如下优点及效果:Compared with the prior art, the present invention has the following advantages and effects:
本发明的多级均匀流场燃料电池,包括设置在燃料电池本体上的阳极流场板、阳极集流板、阳极电极、交换膜、阴极电极、阴极集流板和阴极流场板;阳极集流板与阳极流场板和阳极电极相连,阳极电极和阴极电极通过交换膜隔开,阴极集流板与阴极电极和阴极流场板相连;树状燃料供给支路通过逐级分散的树状流场由燃料分配流路展开,采用树状逐级分散的纵向流入流场,保证电解液能够均匀的进入电极表面,提高电解液反应程度,进一步提升电池效率;The multi-stage uniform flow field fuel cell of the present invention comprises an anode flow field plate, an anode current collector plate, an anode electrode, an exchange membrane, a cathode electrode, a cathode current collector plate and a cathode flow field plate arranged on the fuel cell body; The flow plate is connected with the anode flow field plate and the anode electrode, the anode electrode and the cathode electrode are separated by an exchange membrane, and the cathode current collector plate is connected with the cathode electrode and the cathode flow field plate; The flow field is expanded by the fuel distribution flow path, and the vertical inflow field with a tree-like dispersion is adopted to ensure that the electrolyte can enter the electrode surface uniformly, improve the reaction degree of the electrolyte, and further improve the efficiency of the battery;
同时,阵列状产物排出支路均匀分布连接在产物回收流路上,采用与流入流场相结合的阵列分布纵向流出流场,保证电解液在反应完成后能够顺流流出电极,保证电极侧燃料始终均匀高浓度,避免了燃料与产物的掺混。At the same time, the array-shaped product discharge branches are evenly distributed and connected to the product recovery flow path, and an array combined with the inflow flow field is used to distribute the longitudinal outflow flow field to ensure that the electrolyte can flow out of the electrode downstream after the reaction is completed, and to ensure that the fuel on the electrode side always flows Uniform high concentration, avoiding the mixing of fuel and product.
进一步,所述多条树状燃料供给支路出口和多条阵列状产物排出支路进口等间距间隔设置,燃料反应完成后,由每个树状燃料供给支路出口流入的燃料从距离较近的阵列状产物排出支路入口流出,汇流至产物回收流路排出,进一步降低进出口之间的压差,降低电池额外泵功,提高电池效率。Further, the plurality of tree-shaped fuel supply branch outlets and the plurality of array-shaped product discharge branch inlets are arranged at equal intervals, and after the fuel reaction is completed, the fuel flowing in from the outlet of each tree-shaped fuel supply branch is closer from the distance. The array-shaped product discharge branch flows out from the inlet, and converges to the product recovery flow path for discharge, which further reduces the pressure difference between the inlet and outlet, reduces the extra pump work of the battery, and improves the battery efficiency.
附图说明Description of drawings
图1是本发明燃料电池结构示意图;Fig. 1 is a schematic diagram of the structure of the fuel cell of the present invention;
图2是本发明燃料电池集流板侧视图;Figure 2 is a side view of a fuel cell current collector plate of the present invention;
图中,1-阳极流场板,2-阳极集流板,3-阳极电极,4-交换膜,5-阴极电极,6-阴极集流板,7-阴极流场板,8-燃料进口,9-燃料分配流路,10-树状燃料供给支路,11-阵列状产物排出支路,12-产物回收流路,13-产物出口。In the figure, 1-anode flow field plate, 2-anode current collector plate, 3-anode electrode, 4-exchange membrane, 5-cathode electrode, 6-cathode current collector plate, 7-cathode flow field plate, 8-fuel inlet , 9-fuel distribution flow path, 10-tree fuel supply branch, 11-array product discharge branch, 12-product recovery flow path, 13-product outlet.
具体实施方式Detailed ways
下面结合附图和具体实施例对本发明作进一步详细描述,但不作为对本发明的限定。The present invention will be described in further detail below with reference to the accompanying drawings and specific embodiments, but it is not intended to limit the present invention.
参见图1-2,本发明的多级均匀流场燃料电池,包括设置在燃料电池本体上的阳极流场板1、阳极集流板2、阳极电极3、交换膜4、阴极电极5、阴极集流板6和阴极流场板7;阳极集流板2与阳极流场板1和阳极电极3相连,阳极电极3和阴极电极5通过交换膜4隔开,阴极集流板6与阴极电极5和阴极流场板7相连。1-2, the multi-stage uniform flow field fuel cell of the present invention includes an anode
阳极流场板1为设置有燃料进口8、燃料分配流路9、树状燃料供给支路10、阵列状产物排出支路11、产物回收流路12和产物出口13的流场板,其中树状燃料供给支路10通过逐级分散的树状流场由燃料分配流路9展开,阵列状产物排出支路11均匀分布连接在产物回收流路12上。The anode
燃料进口8为燃料分配流路9与燃料电池外侧相连的进口,树状燃料供给支路10进口与燃料分配流路9相连,树状燃料供给支路10出口通过阳极集流板2与阳极电极3相连,阵列状产物排出支路11进口通过阳极集流板2与阳极电极3相连,阵列状产物排出支路11出口与产物回收流路12相连,树状燃料供给支路10和阵列状产物排出支路11为位于阳极流场板1中互相交错不连通的管路,产物出口13为产物回收流路12与燃料电池外侧相连的出口。The
产物回收流路12纵向设置在阳极流场板1中,产物出口13位于阳极流场板1顶部,燃料进口8位于阳极流场板1侧壁上。The product
多条树状燃料供给支路10出口和多条阵列状产物排出支路11进口等间距间隔设置。The outlets of a plurality of tree-shaped
阳极集流板2为具有阵列分布孔的平板,阳极集流板2中孔道与树状燃料供给支路10出口及阵列状产物排出支路11进口相连通,阴极集流板6为与阴极流场板7流道相对应的具有孔道的平板。阴极流场板7为具有蛇形流道、平行流道、非连续型流道、交指型流道等的平板。The anode
其中燃料为具有化学能且能够转化为电能的液态溶液,包括CH3OH、CH3CH2OH、CO(NH2)2、NaBH4、HCOONa等溶液。The fuel is a liquid solution with chemical energy and can be converted into electrical energy, including solutions such as CH 3 OH, CH 3 CH 2 OH, CO(NH 2 ) 2 , NaBH 4 , and HCOONa.
阳极流场板1和阴极流场板7所用材料具备燃料电池所需要的机械强度及对于所用电解液的耐腐蚀性,包括石墨等无机非金属材料、不锈钢等金属复合材料、聚甲基丙烯酸甲酯等有机高分子材料。The materials used for the anode
阳极集流板2和阴极集流板6材料为石墨等无机非金属或不锈钢等金属的导电材料。The materials of the anode
阳极电极3和阴极电极5为涂覆有相应催化剂具有多孔结构的导电金属材料或碳材料;交换膜4为阳离子交换膜、阴离子交换膜或中性交换膜;The
树状燃料供给支路10为二叉树状逐级分散流场,即树状燃料供给支路可以为由1条电解液供给流路以90°旋转阵列分为4条支路,4条支路进一步分为16条支路,通过“1-4-16”逐级分散方式使电解液进入电极更加均匀;阵列状产物排出支路11以“3×3”阵列分布于电极外侧。The dendritic
一种多级均匀流场燃料电池工作方法包括以下步骤:A working method of a multi-level uniform flow field fuel cell comprises the following steps:
步骤S100:燃料均匀分配进入电极:Step S100: The fuel is evenly distributed into the electrodes:
燃料电池未反应的燃料通过燃料进口8进入燃料电池阳极侧,在泵功的作用下通过燃料分配流路9均匀分配到树状燃料供给支路10,进入阳极电极3中;同时,氧化剂以主动或被动的方式在依次通过阴极流场板7和阴极集流板6进入阴极电极5中;The unreacted fuel of the fuel cell enters the anode side of the fuel cell through the
步骤S200:电池放电反应:Step S200: battery discharge reaction:
以酸性燃料电池为例,燃料在阳极电极3表面进行氧化反应并产生质子,失去电子并升高价位,所失去的电子经由阳极电极3、阳极集流板2通过外电路进入阳极侧,在电场作用下质子通过交换膜4进入阴极侧;电子通过外电路经过阴极集流板6到达阴极电极3表面,氧化剂和质子在阳极表面发生还原反应得到电子降低价位,由此实现电池一次的放电反应;Taking the acid fuel cell as an example, the fuel undergoes an oxidation reaction on the surface of the
步骤S300:产物顺流流出电池:Step S300: The product flows out of the battery downstream:
燃料反应完成后,由每个树状燃料供给支路10出口流入的燃料经过阳极电极3由阵列状产物排出支路11入口顺流流出,进一步电解液有阵列状产物排出支路11汇流至产物回收流路12通过产物出口13排出。After the fuel reaction is completed, the fuel flowing in from the outlet of each dendritic
本发明相对于现有技术,采用一种新型二叉树状逐级分散的纵向流入流场,保证电解液能够均匀的进入电极表面,提高电解液反应程度,进一步提升电池效率;同时本发明采用与流入流场相结合的阵列分布纵向流出流场,保证电解液在反应完成后能够顺流流出电极,保证电极侧燃料始终均匀高浓度,避免了燃料产物的掺混。Compared with the prior art, the present invention adopts a novel binary tree-like dispersed longitudinal inflow field to ensure that the electrolyte can enter the electrode surface uniformly, improve the reaction degree of the electrolyte, and further improve the battery efficiency; at the same time, the present invention adopts and inflow The array combined with the flow field distributes the longitudinal outflow flow field, ensuring that the electrolyte can flow out of the electrode downstream after the reaction is completed, ensuring that the fuel on the electrode side is always uniform and high in concentration, and avoiding the mixing of fuel products.
最后应该说明的是:以上实施例仅用于说明本发明的技术方案而非对其限制,尽管参照上述实施例对本发明进行了详细说明,所属领域的普通技术人员应当理解:依然可以对本发明的具体实施方式进行修改或者等同替换,而未脱离本发明精神和范围的任何修改或者等同替换,其均应涵盖在本权利要求范围当中。Finally, it should be noted that the above embodiments are only used to illustrate the technical solutions of the present invention and not to limit them. Although the present invention has been described in detail with reference to the above embodiments, those of ordinary skill in the art should understand that: Modifications or equivalent substitutions are made to the specific embodiments, and any modifications or equivalent substitutions that do not depart from the spirit and scope of the present invention shall all be included in the scope of the present claims.
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