[go: up one dir, main page]

CN108574107A - Method for Improving Conductivity and Corrosion Resistance of Fuel Cell Bipolar Plate Carbide Coating - Google Patents

Method for Improving Conductivity and Corrosion Resistance of Fuel Cell Bipolar Plate Carbide Coating Download PDF

Info

Publication number
CN108574107A
CN108574107A CN201810219089.9A CN201810219089A CN108574107A CN 108574107 A CN108574107 A CN 108574107A CN 201810219089 A CN201810219089 A CN 201810219089A CN 108574107 A CN108574107 A CN 108574107A
Authority
CN
China
Prior art keywords
metal
coating
carbide coating
carbide
etching
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.)
Pending
Application number
CN201810219089.9A
Other languages
Chinese (zh)
Inventor
易培云
黎焕明
彭林法
邱殿凯
来新民
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shanghai Jiao Tong University
Original Assignee
Shanghai Jiao Tong University
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Shanghai Jiao Tong University filed Critical Shanghai Jiao Tong University
Priority to CN201810219089.9A priority Critical patent/CN108574107A/en
Publication of CN108574107A publication Critical patent/CN108574107A/en
Priority to PCT/CN2019/070161 priority patent/WO2019174373A1/en
Pending legal-status Critical Current

Links

Classifications

    • 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
    • H01M8/0206Metals or alloys
    • 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
    • H01M8/0206Metals or alloys
    • H01M8/0208Alloys
    • H01M8/021Alloys based on iron
    • 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
    • H01M8/0213Gas-impermeable carbon-containing materials
    • 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
    • H01M8/0215Glass; Ceramic materials
    • 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
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Sustainable Energy (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Sustainable Development (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Composite Materials (AREA)
  • Ceramic Engineering (AREA)
  • Fuel Cell (AREA)
  • Physical Vapour Deposition (AREA)
  • ing And Chemical Polishing (AREA)

Abstract

The present invention relates to improve fuel battery double plates carbide coating conduction and corrosion proof method, it is included in metal bipolar plate surface and is sequentially depositing intermediate metal and metal-carbide coating, then processing is performed etching to coating cated bipolar plates, change the surface texture and constituent of carbide coating, finally through over cleaning, the carbide coating that drying obtains corrosion resistance and electric conductivity improves.Compared with prior art, the present invention uses optimization of the lithographic technique to coating performance on the basis of being coated with coating on metal polar plate, coupling influence when adjusting each parameter size when prepared by coating is avoided, therefore can be applied to further improving to reach the job requirement of fuel cell for fuel battery double plates carbide coating performance.

Description

改善燃料电池双极板碳化物涂层导电及耐蚀性的方法Method for Improving Conductivity and Corrosion Resistance of Fuel Cell Bipolar Plate Carbide Coating

技术领域technical field

本发明属于燃料电池技术领域,尤其是涉及一种改善燃料电池双极板碳化物涂层导电及耐蚀性的方法。The invention belongs to the technical field of fuel cells, in particular to a method for improving the conductivity and corrosion resistance of a carbide coating on a fuel cell bipolar plate.

背景技术Background technique

质子交换膜燃料电池(Proton Exchange Membrane Fuel Cell,PEMFC)由于其转换效率高、对环境无污染、工作温度低、工作寿命长等特点,在交通、国防、电子产品等领域得到了广泛的应用。在质子交换膜燃料电池组成结构中双极板占去了大部分的空间与成本,同时燃料电池的服役环境是一种含SO4 2-,Cl-,F-等离子的高温(60~90℃)、强酸性(pH=1~3)环境,因此对双极板的物理性能及化学性能提出了更高的要求:理想的双极板材料必须是电和热的良导体,具有良好的阻气性,在一定工作温度和电位范围内具有良好的耐腐蚀性,密度低,强度高,并且易于加工成型和大批量生产。传统的金属材料具有良好的导电性、导热性,机械性能优异,适合大批量生产,是燃料电池双极板材料的首选,但金属极板在燃料电池工作环境中会发生严重腐蚀,造成金属极板中Cr+,Ni+等金属离子析出,导致质子交换膜污染及催化剂降解,从而降低燃料电池使用寿命,而且在酸性环境中金属表面极易形成钝化膜增大极板和气体扩散层接触电阻,导致电池输出功率的下降。因此在金属极板表面制备耐腐蚀和高导电性的涂层是改善金属极板性能的有效途径。Proton Exchange Membrane Fuel Cell (PEMFC) has been widely used in the fields of transportation, national defense, and electronic products due to its high conversion efficiency, no pollution to the environment, low operating temperature, and long operating life. In the composition structure of proton exchange membrane fuel cell, the bipolar plate occupies most of the space and cost, and the service environment of the fuel cell is a high temperature (60~90℃) containing SO 4 2- , Cl - , F - plasma ), strongly acidic (pH=1~3) environment, so higher requirements are placed on the physical and chemical properties of the bipolar plate: the ideal bipolar plate material must be a good conductor of electricity and heat, with good resistance It has good corrosion resistance within a certain working temperature and potential range, low density, high strength, and is easy to process and mass produce. Traditional metal materials have good electrical conductivity, thermal conductivity, and excellent mechanical properties. They are suitable for mass production and are the first choice for fuel cell bipolar plate materials. However, metal plates will be severely corroded in the working environment of fuel cells, causing metal poles The precipitation of metal ions such as Cr + and Ni + in the plate will lead to the pollution of the proton exchange membrane and the degradation of the catalyst, thereby reducing the service life of the fuel cell, and in the acidic environment, the metal surface is very easy to form a passivation film to increase the contact between the plate and the gas diffusion layer resistance, resulting in a drop in battery output power. Therefore, preparing a corrosion-resistant and high-conductivity coating on the surface of the metal plate is an effective way to improve the performance of the metal plate.

目前应用于金属双极板的涂层主要包括石墨涂层、贵金属涂层、导电聚合物涂层以及金属陶瓷涂层。石墨涂层和贵金属涂层虽然具有良好的化学稳定性以及导电性,但前者沉积速率过慢导致时间成本过高,后者也由于其过高的材料成本而不适于大批量生产;导电聚合物涂层的化学性能并不十分稳定,而且与基体的结合程度无法满足要求。而金属陶瓷涂层,尤其是金属碳化物涂层由于其优异的耐腐蚀性能和导电性能、以及沉积速率快,制备成本低在实际生产中得到了广泛的应用,因此在此基础上进一步提高涂层的性能也是目前研究热点。在金属碳化物涂层耐腐蚀性和导电性能的优化方面,目前主要可以通过以下三个途径来实现:(1)改变金属材料(如Cr,Ti,Zr,Nb等)及工艺参数从而确定拥有最佳性能的金属碳化物中各组成成分的比例;(2)在碳化物涂层中掺杂其它元素(如N或者其它金属);(3)通过物理或化学方法改变涂层的表面结构及组成成分。前两种方法需要重新调试参数制备新的碳化物涂层,而最后一种方法则可以直接在现有的碳化物涂层基础上对其性能进行改善,可以节约大量的时间及材料成本。其中刻蚀工艺是一种通过改变涂层表面结构从而改善涂层性能的有效方法,包括湿法刻蚀及干法刻蚀。刻蚀过程主要包括以下三个步骤:反应物扩散到反应表面,化学反应的进行以及反应产物的剥离。如图1和图2所示,通过刻蚀改变金属碳化物涂层的表面结构及组成成分,除去涂层中部分金属元素,降低服役过程中金属离子的逸出,使更多的导电性颗粒暴露在表面,从而有效地提高涂层的导电性及耐腐蚀性。The coatings currently applied to metal bipolar plates mainly include graphite coatings, noble metal coatings, conductive polymer coatings, and cermet coatings. Although graphite coating and noble metal coating have good chemical stability and electrical conductivity, the deposition rate of the former is too slow, resulting in high time cost, and the latter is not suitable for mass production due to its high material cost; conductive polymers The chemical properties of the coating are not very stable, and the degree of bonding with the substrate cannot meet the requirements. Cermet coatings, especially metal carbide coatings, have been widely used in actual production due to their excellent corrosion resistance and electrical conductivity, fast deposition rate, and low preparation cost. Layer performance is also a research hotspot at present. The optimization of corrosion resistance and electrical conductivity of metal carbide coatings can be achieved mainly through the following three approaches: (1) Change the metal materials (such as Cr, Ti, Zr, Nb, etc.) The ratio of each component in the metal carbide with the best performance; (2) doping other elements (such as N or other metals) in the carbide coating; (3) changing the surface structure of the coating by physical or chemical methods and Composition. The first two methods need to readjust the parameters to prepare a new carbide coating, while the last method can directly improve the performance of the existing carbide coating, which can save a lot of time and material costs. Among them, the etching process is an effective method to improve the performance of the coating by changing the surface structure of the coating, including wet etching and dry etching. The etching process mainly includes the following three steps: the diffusion of the reactant to the reaction surface, the conduction of the chemical reaction, and the stripping of the reaction product. As shown in Figure 1 and Figure 2, the surface structure and composition of the metal carbide coating are changed by etching, part of the metal elements in the coating are removed, the escape of metal ions during service is reduced, and more conductive particles Exposed on the surface, thereby effectively improving the electrical conductivity and corrosion resistance of the coating.

专利公开号CN102800871A公开了一种采用非平衡磁控溅射技术制备碳铬阶梯镀层的方法,通过调整一系列的工艺参数从而改变涂层中的组成成分,进一步改善金属双极板的耐腐蚀性能和导电性能。专利公开号CN101626082B提出在薄板表面改性之前采用化学腐蚀去除钝化膜以及沉积导电陶瓷层之后在其表面加镀银层并且涂覆一层镀银保护膜。专利公开号CN101918619A公开了一种制造高导电性表面的方法,包括在耐腐蚀金属衬底或涂层表面利用热喷射、选择性镀层、选择性蚀刻等技术沉积耐腐蚀性颗粒,导电性颗粒或者包含这些颗粒的金属,而后使这些颗粒暴露出来从而提高金属表面导电性。专利公开号CN103050712A公开了一种改善镀有碳化铬不锈钢双极板耐腐蚀性能的方法,即对覆有涂层的不锈钢双极板进行脱油、脱脂处理并置于稀土钝化液KMnO4+Ce(NO3)3·6H2+Mg(NO3)2中处理一段时间,可以显著降低双极板的腐蚀电流密度。专利公开号CN106929856A采用氢氟酸对镍表面进行水浴刻蚀,提高其表面粗糙度从而提高表面的疏水性能。专利公开号CN102051598A公开了一种通过氢氟酸和硝酸的混合液的超声浸泡刻蚀方法提高了钛和氮化钛薄膜之间的结合力。然而上述公开专利中针对金属碳化物涂层性能的改进方法工艺都较为复杂,增大了涂层制备的成本,而且并没有直接采用刻蚀工艺对金属碳化物涂层的耐腐蚀性及导电性进行改善。Patent Publication No. CN102800871A discloses a method for preparing a carbon-chromium step coating by unbalanced magnetron sputtering technology. By adjusting a series of process parameters to change the composition of the coating, the corrosion resistance of the metal bipolar plate is further improved. and electrical conductivity. Patent Publication No. CN101626082B proposes to use chemical etching to remove the passivation film and deposit a conductive ceramic layer before surface modification of the sheet, and then add a silver-plated layer and coat a silver-plated protective film on the surface. Patent Publication No. CN101918619A discloses a method for manufacturing a highly conductive surface, including depositing corrosion-resistant particles, conductive particles or The metal containing these particles then exposes the particles to increase the conductivity of the metal surface. Patent Publication No. CN103050712A discloses a method for improving the corrosion resistance of chromium carbide-plated stainless steel bipolar plates, that is, degreasing and degreasing the coated stainless steel bipolar plates and placing them in a rare earth passivation solution KMnO 4 + Ce(NO 3 ) 3 ·6H 2 +Mg(NO 3 ) 2 treatment for a period of time can significantly reduce the corrosion current density of the bipolar plate. Patent Publication No. CN106929856A uses hydrofluoric acid to etch the nickel surface in a water bath to increase the surface roughness and thereby improve the hydrophobicity of the surface. Patent Publication No. CN102051598A discloses an ultrasonic immersion etching method using a mixture of hydrofluoric acid and nitric acid to improve the bonding force between titanium and titanium nitride films. However, the methods for improving the performance of metal carbide coatings in the above-mentioned published patents are relatively complicated, which increases the cost of coating preparation, and does not directly use the etching process to improve the corrosion resistance and conductivity of metal carbide coatings. Make improvements.

发明内容Contents of the invention

本发明的目的就是为了克服上述现有技术存在的缺陷而提供一种通过刻蚀方法改善燃料电池双极板金属碳化物涂层耐腐蚀性及导电性能简单有效的方法。The object of the present invention is to provide a simple and effective method for improving the corrosion resistance and electrical conductivity of the metal carbide coating on the fuel cell bipolar plate by etching to overcome the above-mentioned defects in the prior art.

本发明的目的可以通过以下技术方案来实现:The purpose of the present invention can be achieved through the following technical solutions:

改善燃料电池双极板碳化物涂层导电及耐蚀性的方法,包括在金属双极板表面依次沉积金属过渡层和金属碳化物涂层,然后对涂覆有涂层的双极板进行刻蚀处理,改变碳化物涂层的表面结构及组成成分,最后经过清洗,烘干得到耐腐蚀性能和导电性改善的碳化物涂层,具体采用以下步骤:The method for improving the conductivity and corrosion resistance of the carbide coating on the fuel cell bipolar plate comprises depositing a metal transition layer and a metal carbide coating in sequence on the surface of the metal bipolar plate, and then engraving the coated bipolar plate Corrosion treatment to change the surface structure and composition of the carbide coating, and finally after cleaning and drying to obtain a carbide coating with improved corrosion resistance and electrical conductivity, the specific steps are as follows:

1)金属双极板预处理:将金属双极板依次置于乙醇,丙酮中,采用超声清洗并烘干;1) Metal bipolar plate pretreatment: place the metal bipolar plate in ethanol and acetone in sequence, ultrasonically clean and dry;

2)涂层制备:在金属双极板表面沉积金属过渡层及金属碳化物涂层;2) Coating preparation: depositing a metal transition layer and a metal carbide coating on the surface of the metal bipolar plate;

3)涂层刻蚀:将双极板完全浸入事先配置好的化学刻蚀溶液中进行湿法刻蚀或者置于刻蚀设备中干法刻蚀;3) Coating etching: fully immerse the bipolar plate in the pre-configured chemical etching solution for wet etching or dry etching in etching equipment;

4)取出刻蚀后的金属双极板并清洗烘干得到耐腐蚀性和导电性改善的碳化物涂层。4) Take out the etched metal bipolar plate, wash and dry to obtain a carbide coating with improved corrosion resistance and electrical conductivity.

所述的金属双极板的材质包括不锈钢、铝合金或镁合金中的一种,厚度为0.1-2mm。The material of the metal bipolar plate includes one of stainless steel, aluminum alloy or magnesium alloy, and the thickness is 0.1-2mm.

所述的金属过渡层由铬(Cr),钛(Ti),锆(Zr),铌(Nb)和钼(Mo)中的一种金属组成,厚度为5-100nm。The metal transition layer is composed of one metal among chromium (Cr), titanium (Ti), zirconium (Zr), niobium (Nb) and molybdenum (Mo), and the thickness is 5-100nm.

所述金属碳化物涂层为阶梯性涂层或连续性涂层,厚度10-300nm。The metal carbide coating is a stepped coating or a continuous coating with a thickness of 10-300nm.

所述金属碳化物涂层涂覆的金属碳化物包括碳化铬(Cr3C2)、碳化钛(TiC)、碳化锆(ZrC)、碳化铌(NbC)或碳化钼(MoC)中的一种或多种。The metal carbide coated by the metal carbide coating includes one of chromium carbide (Cr 3 C 2 ), titanium carbide (TiC), zirconium carbide (ZrC), niobium carbide (NbC) or molybdenum carbide (MoC) or more.

所述金属碳化物涂层通过磁控溅射法、化学气相沉积、多弧离子镀或电子束蒸发制备得到。The metal carbide coating is prepared by magnetron sputtering, chemical vapor deposition, multi-arc ion plating or electron beam evaporation.

湿法刻蚀采用氢氟酸溶液或者氢氟酸和硝酸的混合液,刻蚀温度为10-70℃,刻蚀时间为5s-20min。通过刻蚀液与涂层之间的化学反应,使涂层中的导电性金属颗粒暴露在涂层表面,降低涂层内部的金属含量,有效地提高涂层的耐腐蚀性和导电性。当刻蚀液浓度过大或者刻蚀时间过长时,会造成涂层的严重损伤而暴露出基底,温度过高则会导致刻蚀液的挥发,而且不易控制刻蚀速度。如果刻蚀液浓度过低,温度过低或者刻蚀时间过短,刻蚀速率过低,对涂层成分的影响很小而无法达到改善效果。Hydrofluoric acid solution or a mixture of hydrofluoric acid and nitric acid is used for wet etching, the etching temperature is 10-70°C, and the etching time is 5s-20min. Through the chemical reaction between the etching solution and the coating, the conductive metal particles in the coating are exposed on the coating surface, reducing the metal content inside the coating, and effectively improving the corrosion resistance and conductivity of the coating. When the concentration of the etchant is too high or the etching time is too long, the coating will be severely damaged and the substrate will be exposed. If the temperature is too high, the etchant will volatilize, and it is difficult to control the etching speed. If the etchant concentration is too low, the temperature is too low or the etching time is too short, and the etching rate is too low, the influence on the composition of the coating is small and the improvement effect cannot be achieved.

所述氢氟酸溶液的质量浓度为0.5%-10%,所述氢氟酸和硝酸的混合液中氢氟酸的质量浓度为0.5%-10%,硝酸的质量浓度为0.1%-20%The mass concentration of the hydrofluoric acid solution is 0.5%-10%, the mass concentration of hydrofluoric acid in the mixed solution of hydrofluoric acid and nitric acid is 0.5%-10%, and the mass concentration of nitric acid is 0.1%-20%.

干法刻蚀采用的工艺气体包括氯气、四氟化碳、四氯化碳、氢气或氧气中的一种或几种。气体流量为10-500sccm,气压为10-1000Pa,刻蚀时间为5min-1h。反应气体在高能放电反应作用下被激活成活性粒子,这些粒子扩散到涂层表面进行反应,形成挥发性物质而去除金属,刻蚀时间过长的话会对涂层造成损伤,过短则无法达到性能改善的效果。The process gas used in dry etching includes one or more of chlorine, carbon tetrafluoride, carbon tetrachloride, hydrogen or oxygen. The gas flow rate is 10-500sccm, the pressure is 10-1000Pa, and the etching time is 5min-1h. The reactive gas is activated into active particles under the action of high-energy discharge reaction. These particles diffuse to the surface of the coating to react and form volatile substances to remove metal. If the etching time is too long, the coating will be damaged, and if it is too short, it will not be able to achieve The effect of performance improvement.

与现有技术相比,本发明在已镀的一层或多层碳化物涂层的基础之上,采用湿法刻蚀或者干法刻蚀改变涂层的表面结构及成分组成,增大涂层的表面粗糙度,从而进一步改善碳化物涂层的耐腐蚀性及其导电性能。相比于现有的一些金属碳化物涂层的制备和性能改善方法,本发明在提升碳化物涂层的耐腐蚀性和导电性能的同时,大大减少了工艺的执行复杂度,降低涂层制备成本,并且对金属极板的机械性能几乎无影响。本发明是在金属极板上镀有涂层的基础上采用刻蚀技术对涂层性能的优化,从而避免了涂层制备时调整各参数大小时的耦合影响,因此可应用于燃料电池双极板碳化物涂层性能的进一步完善以达到燃料电池的工作要求。Compared with the prior art, the present invention uses wet etching or dry etching to change the surface structure and component composition of the coating on the basis of one or more layers of carbide coatings that have been plated, thereby increasing the coating thickness. The surface roughness of the layer, thereby further improving the corrosion resistance and electrical conductivity of the carbide coating. Compared with some existing metal carbide coating preparation and performance improvement methods, the present invention greatly reduces the execution complexity of the process and reduces the coating preparation while improving the corrosion resistance and electrical conductivity of the carbide coating. cost, and has little effect on the mechanical properties of metal plates. The present invention uses etching technology to optimize the performance of the coating on the basis of coating on the metal plate, thereby avoiding the coupling effect when adjusting the size of each parameter during coating preparation, so it can be applied to fuel cell bipolar The performance of the plate carbide coating is further improved to meet the working requirements of the fuel cell.

附图说明Description of drawings

图1为未经处理的金属极板的示意图;Fig. 1 is the schematic diagram of untreated metal pole plate;

图2为刻蚀后的金属极板的示意图;Fig. 2 is the schematic diagram of the metal pole plate after etching;

图3为本发明在不同时间长度下刻蚀后金属双极板的接触电阻;Fig. 3 is the contact resistance of the metal bipolar plate after etching under different lengths of time in the present invention;

图4为本发明在不同浓度下刻蚀后金属双极板腐蚀前后的接触电阻。Fig. 4 is the contact resistance of the metal bipolar plate before and after etching at different concentrations according to the present invention.

图中,1-金属极板、2-金属过渡层、3-金属碳化物层、4-金属碳化物颗粒、5-金属颗粒、6-刻蚀产生的金属离子。In the figure, 1-metal plate, 2-metal transition layer, 3-metal carbide layer, 4-metal carbide particles, 5-metal particles, 6-metal ions generated by etching.

具体实施方式Detailed ways

下面结合具体实施例对本发明进行详细说明。以下实施例将有助于本领域的技术人员进一步理解本发明,但不以任何形式限制本发明。应当指出的是,对本领域的普通技术人员来说,在不脱离本发明构思的前提下,还可以做出若干变形和改进。这些都属于本发明的保护范围。The present invention will be described in detail below in conjunction with specific embodiments. The following examples will help those skilled in the art to further understand the present invention, but do not limit the present invention in any form. It should be noted that those skilled in the art can make several modifications and improvements without departing from the concept of the present invention. These all belong to the protection scope of the present invention.

实施例1:Example 1:

以不锈钢双极板为基体,在其表面制备碳化钛涂层,工艺过程如下:The titanium carbide coating is prepared on the surface of the stainless steel bipolar plate as the substrate, and the process is as follows:

1)极板预处理:依次使用去离子水、丙酮、无水乙醇对不锈钢双极板表面超声清洗并将其烘干;1) Plate pretreatment: use deionized water, acetone, and absolute ethanol in sequence to ultrasonically clean the surface of the stainless steel bipolar plate and dry it;

2)将预处理过的不锈钢双极板悬挂于非平衡磁控溅射离子镀炉腔内的行星转架台上,保持转架转速为4r/min,抽真空至本底真空3*10-5Torr后,充入氩气并保持工作气压为4*10-4Torr,不锈钢基体施加偏压-500V,使离子对基体表面持续轰击,清楚表面上的钝化层,清洗时间30min;2) Hang the pretreated stainless steel bipolar plate on the planetary turret platform in the unbalanced magnetron sputtering ion plating furnace chamber, keep the turret speed at 4r/min, and evacuate to the background vacuum of 3*10 -5 After Torr, fill with argon and keep the working pressure at 4*10 -4 Torr, apply a bias voltage of -500V to the stainless steel substrate, so that the ions continuously bombard the surface of the substrate, clear the passivation layer on the surface, and clean for 30 minutes;

3)通入20sccm氩气作为保护气体,并通入20sccm反应气体乙炔30min,保持基体偏压在-100V,开启钛靶电流,在不锈钢极板表面反应溅射沉积碳化钛涂层;3) Introduce 20 sccm of argon as a protective gas, and 20 sccm of reaction gas acetylene for 30 minutes, keep the substrate bias at -100V, turn on the titanium target current, and deposit a titanium carbide coating on the surface of the stainless steel plate by reactive sputtering;

4)关闭靶电流和通气口,冷却20min,得到所需的碳化钛涂层。4) Turn off the target current and the air vent, and cool for 20 minutes to obtain the desired titanium carbide coating.

如图3所示,所述的金属双极板初始接触电阻为7.84mΩ·cm2,在pH=3的硫酸中经过恒电位1.6V(vs.SHE)腐蚀1h后接触电阻增大到31.07mΩ·cm2As shown in Figure 3, the initial contact resistance of the metal bipolar plate is 7.84mΩ·cm 2 , and the contact resistance increases to 31.07mΩ after being corroded for 1 hour at a constant potential of 1.6V (vs. SHE) in sulfuric acid with pH=3 • cm 2 .

实施例2:Example 2:

以不锈钢双极板为基体,在其表面制备碳化钛涂层,并通过湿法刻蚀提升碳化钛涂层的耐腐蚀性和导电性,工艺过程如下:The stainless steel bipolar plate is used as the substrate, and the titanium carbide coating is prepared on the surface, and the corrosion resistance and conductivity of the titanium carbide coating are improved by wet etching. The process is as follows:

1)极板预处理:依次使用去离子水、丙酮、无水乙醇对不锈钢双极板表面超声清洗并将其烘干;1) Plate pretreatment: use deionized water, acetone, and absolute ethanol in sequence to ultrasonically clean the surface of the stainless steel bipolar plate and dry it;

2)将预处理过的不锈钢双极板悬挂于非平衡磁控溅射离子镀炉腔内的行星转架台上,抽真空至本底真空后,充入氩气,并在不锈钢基体上施加偏压,使离子对基体表面持续轰击,清洗时间30min;2) Suspend the pretreated stainless steel bipolar plate on the planetary turret platform in the unbalanced magnetron sputtering ion plating furnace cavity, vacuumize to the background vacuum, fill it with argon, and apply bias on the stainless steel substrate. pressure, so that the ions continue to bombard the surface of the substrate, and the cleaning time is 30 minutes;

3)向真空容器中同时通入工作气体和反应气体,通过溅射金属靶在不锈钢极板表面反应溅射沉积碳化钛涂层,溅射时间30min;3) Pass the working gas and the reaction gas into the vacuum container at the same time, and deposit the titanium carbide coating on the surface of the stainless steel plate by sputtering the metal target, and the sputtering time is 30 minutes;

4)将镀有碳化钛涂层的金属双极板置于质量分数6%的氢氟酸中浸泡5s后,取出极板清洗并烘干,得到性能改善的碳化钛涂层。4) After immersing the metal bipolar plate coated with titanium carbide coating in 6% hydrofluoric acid for 5 seconds, the plate was taken out, cleaned and dried to obtain a titanium carbide coating with improved properties.

如图3所示,所述的金属双极板初始接触电阻为2.33mΩ·cm2As shown in FIG. 3 , the initial contact resistance of the metal bipolar plate is 2.33 mΩ·cm 2 .

实施例3:Example 3:

以不锈钢双极板为基体,在其表面制备碳化钛涂层,并通过湿法刻蚀提升碳化钛涂层的耐腐蚀性和导电性,工艺过程如下:The stainless steel bipolar plate is used as the substrate, and the titanium carbide coating is prepared on the surface, and the corrosion resistance and conductivity of the titanium carbide coating are improved by wet etching. The process is as follows:

1)极板预处理:依次使用去离子水、丙酮、无水乙醇对不锈钢双极板表面超声清洗并将其烘干;1) Plate pretreatment: use deionized water, acetone, and absolute ethanol in sequence to ultrasonically clean the surface of the stainless steel bipolar plate and dry it;

2)将预处理过的不锈钢双极板悬挂于非平衡磁控溅射离子镀炉腔内的行星转架台上,抽真空至本底真空后,充入氩气,并在不锈钢基体上施加偏压,使离子对基体表面持续轰击,清洗时间30min;2) Suspend the pretreated stainless steel bipolar plate on the planetary turret platform in the unbalanced magnetron sputtering ion plating furnace cavity, vacuumize to the background vacuum, fill it with argon, and apply bias on the stainless steel substrate. pressure, so that the ions continue to bombard the surface of the substrate, and the cleaning time is 30 minutes;

3)向真空容器中同时通入工作气体和反应气体,通过溅射金属靶在不锈钢极板表面反应溅射沉积碳化钛涂层,溅射时间30min;3) Pass the working gas and the reaction gas into the vacuum container at the same time, and deposit the titanium carbide coating on the surface of the stainless steel plate by sputtering the metal target, and the sputtering time is 30 minutes;

4)将镀有碳化钛涂层的金属双极板置于质量分数6%的氢氟酸中浸泡10s后,取出极板清洗并烘干,得到性能改善的碳化钛涂层。4) After immersing the metal bipolar plate coated with titanium carbide coating in 6% hydrofluoric acid for 10 seconds, the plate was taken out, cleaned and dried to obtain a titanium carbide coating with improved properties.

如图3所示,所述的金属双极板初始接触电阻为2.51mΩ·cm2As shown in FIG. 3 , the initial contact resistance of the metal bipolar plate is 2.51 mΩ·cm 2 .

实施例4:Example 4:

以不锈钢双极板为基体,在其表面制备碳化钛涂层,并通过湿法刻蚀提升碳化钛涂层的耐腐蚀性和导电性,工艺过程如下:The stainless steel bipolar plate is used as the substrate, and the titanium carbide coating is prepared on the surface, and the corrosion resistance and conductivity of the titanium carbide coating are improved by wet etching. The process is as follows:

1)极板预处理:依次使用去离子水、丙酮、无水乙醇对不锈钢双极板表面超声清洗并将其烘干;1) Plate pretreatment: use deionized water, acetone, and absolute ethanol in sequence to ultrasonically clean the surface of the stainless steel bipolar plate and dry it;

2)将预处理过的不锈钢双极板悬挂于非平衡磁控溅射离子镀炉腔内的行星转架台上,抽真空至本底真空后,充入氩气,并在不锈钢基体上施加偏压,使离子对基体表面持续轰击,清洗时间30min;2) Suspend the pretreated stainless steel bipolar plate on the planetary turret platform in the unbalanced magnetron sputtering ion plating furnace cavity, vacuumize to the background vacuum, fill it with argon, and apply bias on the stainless steel substrate. pressure, so that the ions continue to bombard the surface of the substrate, and the cleaning time is 30 minutes;

3)向真空容器中同时通入工作气体和反应气体,通过溅射金属靶在不锈钢极板表面反应溅射沉积碳化钛涂层,溅射时间30min;3) Pass the working gas and the reaction gas into the vacuum container at the same time, and deposit the titanium carbide coating on the surface of the stainless steel plate by sputtering the metal target, and the sputtering time is 30 minutes;

4)将镀有碳化钛涂层的金属双极板置于质量分数6%的氢氟酸中浸泡20s后,取出极板清洗并烘干,得到性能改善的碳化钛涂层。4) After immersing the metal bipolar plate coated with titanium carbide coating in 6% hydrofluoric acid for 20 seconds, take out the plate, clean it and dry it to obtain a titanium carbide coating with improved properties.

如图3所示,所述的金属双极板初始接触电阻为2.72mΩ·cm2As shown in FIG. 3 , the initial contact resistance of the metal bipolar plate is 2.72 mΩ·cm 2 .

实施例5:Example 5:

以不锈钢双极板为基体,在其表面制备碳化钛涂层,并通过湿法刻蚀提升碳化钛涂层的耐腐蚀性和导电性,工艺过程如下:The stainless steel bipolar plate is used as the substrate, and the titanium carbide coating is prepared on the surface, and the corrosion resistance and conductivity of the titanium carbide coating are improved by wet etching. The process is as follows:

1)极板预处理:依次使用去离子水、丙酮、无水乙醇对不锈钢双极板表面超声清洗并将其烘干;1) Plate pretreatment: use deionized water, acetone, and absolute ethanol in sequence to ultrasonically clean the surface of the stainless steel bipolar plate and dry it;

2)将预处理过的不锈钢双极板悬挂于非平衡磁控溅射离子镀炉腔内的行星转架台上,抽真空至本底真空后,充入氩气,并在不锈钢基体上施加偏压,使离子对基体表面持续轰击,清洗时间30min;2) Suspend the pretreated stainless steel bipolar plate on the planetary turret platform in the unbalanced magnetron sputtering ion plating furnace cavity, vacuumize to the background vacuum, fill it with argon, and apply bias on the stainless steel substrate. pressure, so that the ions continue to bombard the surface of the substrate, and the cleaning time is 30 minutes;

3)向真空容器中同时通入工作气体和反应气体,通过溅射金属靶在不锈钢极板表面反应溅射沉积碳化钛涂层,溅射时间30min;3) Pass the working gas and the reaction gas into the vacuum container at the same time, and deposit the titanium carbide coating on the surface of the stainless steel plate by sputtering the metal target, and the sputtering time is 30 minutes;

4)将镀有碳化钛涂层的金属双极板置于质量分数6%的氢氟酸中浸泡30s后,取出极板清洗并烘干,得到性能改善的碳化钛涂层。4) After immersing the metal bipolar plate coated with titanium carbide coating in 6% hydrofluoric acid for 30 seconds, the plate was taken out, cleaned and dried to obtain a titanium carbide coating with improved properties.

如图3所示,所述的金属双极板初始接触电阻为2.73mΩ·cm2As shown in FIG. 3 , the initial contact resistance of the metal bipolar plate is 2.73 mΩ·cm 2 .

实施例6:Embodiment 6:

以不锈钢双极板为基体,在其表面制备碳化钛涂层,并通过湿法刻蚀提升碳化钛涂层的耐腐蚀性和导电性,工艺过程如下:The stainless steel bipolar plate is used as the substrate, and the titanium carbide coating is prepared on the surface, and the corrosion resistance and conductivity of the titanium carbide coating are improved by wet etching. The process is as follows:

1)极板预处理:依次使用去离子水、丙酮、无水乙醇对不锈钢双极板表面超声清洗并将其烘干;1) Plate pretreatment: use deionized water, acetone, and absolute ethanol in sequence to ultrasonically clean the surface of the stainless steel bipolar plate and dry it;

2)将预处理过的不锈钢双极板悬挂于非平衡磁控溅射离子镀炉腔内的行星转架台上,抽真空至本底真空后,充入氩气,并在不锈钢基体上施加偏压,使离子对基体表面持续轰击,清洗时间30min;2) Suspend the pretreated stainless steel bipolar plate on the planetary turret platform in the unbalanced magnetron sputtering ion plating furnace cavity, vacuumize to the background vacuum, fill it with argon, and apply bias on the stainless steel substrate. pressure, so that the ions continue to bombard the surface of the substrate, and the cleaning time is 30 minutes;

3)向真空容器中同时通入工作气体和反应气体,通过溅射金属靶在不锈钢极板表面反应溅射沉积碳化钛涂层,溅射时间30min;3) Pass the working gas and the reaction gas into the vacuum container at the same time, and deposit the titanium carbide coating on the surface of the stainless steel plate by sputtering the metal target, and the sputtering time is 30 minutes;

4)将镀有碳化钛涂层的金属双极板置于质量分数2%的氢氟酸中浸泡10s后,取出极板清洗并烘干,得到性能改善的碳化钛涂层。4) After immersing the metal bipolar plate coated with titanium carbide coating in 2% hydrofluoric acid for 10 seconds, take out the plate, clean it and dry it to obtain a titanium carbide coating with improved properties.

如图4所示,所述的金属双极板初始接触电阻为2.77mΩ·cm2,在pH=3的硫酸中经过恒电位1.6V(vs.SHE)腐蚀1h后接触电阻增大到15.82mΩ·cm2As shown in Figure 4, the initial contact resistance of the metal bipolar plate is 2.77mΩ·cm 2 , and the contact resistance increases to 15.82mΩ after being corroded for 1 hour at a constant potential of 1.6V (vs. SHE) in sulfuric acid with pH=3 • cm 2 .

实施例7:Embodiment 7:

以不锈钢双极板为基体,在其表面制备碳化钛涂层,并通过湿法刻蚀提升碳化钛涂层的耐腐蚀性和导电性,工艺过程如下:The stainless steel bipolar plate is used as the substrate, and the titanium carbide coating is prepared on the surface, and the corrosion resistance and conductivity of the titanium carbide coating are improved by wet etching. The process is as follows:

1)极板预处理:依次使用去离子水、丙酮、无水乙醇对不锈钢双极板表面超声清洗并将其烘干;1) Plate pretreatment: use deionized water, acetone, and absolute ethanol in sequence to ultrasonically clean the surface of the stainless steel bipolar plate and dry it;

2)将预处理过的不锈钢双极板悬挂于非平衡磁控溅射离子镀炉腔内的行星转架台上,抽真空至本底真空后,充入氩气,并在不锈钢基体上施加偏压,使离子对基体表面持续轰击,清洗时间30min;2) Suspend the pretreated stainless steel bipolar plate on the planetary turret platform in the unbalanced magnetron sputtering ion plating furnace cavity, vacuumize to the background vacuum, fill it with argon, and apply bias on the stainless steel substrate. pressure, so that the ions continue to bombard the surface of the substrate, and the cleaning time is 30 minutes;

3)向真空容器中同时通入工作气体和反应气体,通过溅射金属靶在不锈钢极板表面反应溅射沉积碳化钛涂层,溅射时间30min;3) Pass the working gas and the reaction gas into the vacuum container at the same time, and deposit the titanium carbide coating on the surface of the stainless steel plate by sputtering the metal target, and the sputtering time is 30 minutes;

4)将镀有碳化钛涂层的金属双极板置于质量分数4%的氢氟酸中浸泡10s后,取出极板清洗并烘干,得到性能改善的碳化钛涂层。4) After immersing the metal bipolar plate coated with titanium carbide coating in 4% hydrofluoric acid for 10 seconds, the plate was taken out, cleaned and dried to obtain a titanium carbide coating with improved properties.

如图4所示,金属双极板初始接触电阻为2.32mΩ·cm2,在pH=3的硫酸中经过恒电位1.6V(vs.SHE)腐蚀1h后接触电阻增大到17.16mΩ·cm2As shown in Figure 4, the initial contact resistance of the metal bipolar plate is 2.32mΩ·cm 2 , and the contact resistance increases to 17.16mΩ·cm 2 after being corroded for 1 hour at a constant potential of 1.6V (vs. SHE) in sulfuric acid with pH=3 .

上述实施例以本发明技术方案为前提进行实施,给出了详细的实施方式和具体的操作过程,其中在实施例3的条件下——6%氢氟酸刻蚀10s后,金属碳化物涂层具有最佳的耐腐蚀性和导电性,腐蚀前的接触电阻为2.51mΩ·cm2,腐蚀后接触电阻为6.72mΩ·cm2,均满足燃料电池双极板接触电阻小于10mΩ·cm2的要求。The above-mentioned examples are implemented on the premise of the technical solution of the present invention, and detailed implementation methods and specific operation processes are provided, wherein under the conditions of Example 3-after 6% hydrofluoric acid etching for 10s, the metal carbide coating The layer has the best corrosion resistance and electrical conductivity, the contact resistance before corrosion is 2.51mΩ·cm 2 , and the contact resistance after corrosion is 6.72mΩ·cm 2 , both of which meet the requirement that the contact resistance of fuel cell bipolar plates is less than 10mΩ·cm 2 Require.

实施例8:Embodiment 8:

未经过湿法刻蚀或者干法刻蚀的金属极板的结构如图1所示,包括金属极板1,涂覆在金属极板1上的金属过渡层2以及金属碳化物层3,在金属碳化物层3内含有金属碳化物颗粒4以及金属颗粒5。The structure of the metal pole plate without wet etching or dry etching is shown in Figure 1, including the metal pole plate 1, the metal transition layer 2 and the metal carbide layer 3 coated on the metal pole plate 1, in The metal carbide layer 3 contains metal carbide particles 4 and metal particles 5 .

通过湿法刻蚀或者干法刻蚀的金属极板的结构如图2所示,与图1相比,经过刻蚀后,金属碳化物层3中的大部分金属颗粒5形成金属离子6而进入刻蚀液或者形成挥发性物质而被去除,造成导电性金属颗粒暴露在涂层表面从而导电性得到提高。而金属碳化物颗粒4所受刻蚀影响较小,造成涂层中金属碳化物含量的增加,进一步提高涂层的耐腐蚀性能。The structure of the metal pole plate by wet etching or dry etching is shown in Figure 2. Compared with Figure 1, after etching, most of the metal particles 5 in the metal carbide layer 3 form metal ions 6 and Enter the etching solution or form volatile substances and be removed, causing the conductive metal particles to be exposed on the surface of the coating, thereby improving the conductivity. However, metal carbide particles 4 are less affected by etching, resulting in an increase in the content of metal carbides in the coating, further improving the corrosion resistance of the coating.

实施例9:Embodiment 9:

改善燃料电池双极板碳化物涂层导电及耐蚀性的方法,包括在金属双极板表面依次沉积金属过渡层和金属碳化物涂层,然后对涂覆有涂层的双极板进行刻蚀处理,改变碳化物涂层的表面结构及组成成分,最后经过清洗,烘干得到耐腐蚀性能和导电性改善的碳化物涂层,具体采用以下步骤:The method for improving the conductivity and corrosion resistance of the carbide coating on the fuel cell bipolar plate comprises depositing a metal transition layer and a metal carbide coating in sequence on the surface of the metal bipolar plate, and then engraving the coated bipolar plate Corrosion treatment to change the surface structure and composition of the carbide coating, and finally after cleaning and drying to obtain a carbide coating with improved corrosion resistance and electrical conductivity, the specific steps are as follows:

1)金属双极板预处理:将金属双极板依次置于乙醇,丙酮中,采用超声清洗并烘干;1) Metal bipolar plate pretreatment: place the metal bipolar plate in ethanol and acetone in sequence, ultrasonically clean and dry;

2)涂层制备:在金属双极板表面沉积金属过渡层及金属碳化物涂层,其中金属碳化物涂层为阶梯性涂层,厚度10nm,涂覆的金属碳化物包括碳化铬(Cr3C2)、碳化钛(TiC),通过磁控溅射法制备得到;2) Coating preparation: Deposit a metal transition layer and a metal carbide coating on the surface of the metal bipolar plate, wherein the metal carbide coating is a stepped coating with a thickness of 10nm, and the coated metal carbide includes chromium carbide ( Cr3 C 2 ), titanium carbide (TiC), prepared by magnetron sputtering;

3)涂层刻蚀:将双极板完全浸入事先配置好的质量浓度为0.5%氢氟酸溶液中进行湿法刻蚀,刻蚀温度为10℃,刻蚀时间为20min;3) Coating etching: The bipolar plate is completely immersed in a pre-configured hydrofluoric acid solution with a mass concentration of 0.5% for wet etching, the etching temperature is 10°C, and the etching time is 20 minutes;

4)取出刻蚀后的金属双极板并清洗烘干得到耐腐蚀性和导电性改善的碳化物涂层。4) Take out the etched metal bipolar plate, wash and dry to obtain a carbide coating with improved corrosion resistance and electrical conductivity.

实施例10:Example 10:

改善燃料电池双极板碳化物涂层导电及耐蚀性的方法,包括在金属双极板表面依次沉积金属过渡层和金属碳化物涂层,然后对涂覆有涂层的双极板进行刻蚀处理,改变碳化物涂层的表面结构及组成成分,最后经过清洗,烘干得到耐腐蚀性能和导电性改善的碳化物涂层,具体采用以下步骤:The method for improving the conductivity and corrosion resistance of the carbide coating on the fuel cell bipolar plate comprises depositing a metal transition layer and a metal carbide coating in sequence on the surface of the metal bipolar plate, and then engraving the coated bipolar plate Corrosion treatment to change the surface structure and composition of the carbide coating, and finally after cleaning and drying to obtain a carbide coating with improved corrosion resistance and electrical conductivity, the specific steps are as follows:

1)金属双极板预处理:将金属双极板依次置于乙醇,丙酮中,采用超声清洗并烘干;1) Metal bipolar plate pretreatment: place the metal bipolar plate in ethanol and acetone in sequence, ultrasonically clean and dry;

2)涂层制备:在金属双极板表面沉积金属过渡层及金属碳化物涂层,其中金属碳化物涂层为阶梯性涂层,厚度80nm,涂覆的金属碳化物为碳化锆(ZrC),通过化学气相沉积制备得到;2) Coating preparation: Deposit a metal transition layer and a metal carbide coating on the surface of the metal bipolar plate, wherein the metal carbide coating is a stepped coating with a thickness of 80nm, and the coated metal carbide is zirconium carbide (ZrC) , prepared by chemical vapor deposition;

3)涂层刻蚀:将双极板完全浸入质量浓度为10%的氢氟酸以及0.1%硝酸所构成的化学刻蚀溶液中进行湿法刻蚀;3) Coating etching: the bipolar plate is completely immersed in a chemical etching solution composed of 10% hydrofluoric acid and 0.1% nitric acid for wet etching;

4)取出刻蚀后的金属双极板并清洗烘干得到耐腐蚀性和导电性改善的碳化物涂层。4) Take out the etched metal bipolar plate, wash and dry to obtain a carbide coating with improved corrosion resistance and electrical conductivity.

实施例11:Example 11:

改善燃料电池双极板碳化物涂层导电及耐蚀性的方法,包括在金属双极板表面依次沉积金属过渡层和金属碳化物涂层,然后对涂覆有涂层的双极板进行刻蚀处理,改变碳化物涂层的表面结构及组成成分,最后经过清洗,烘干得到耐腐蚀性能和导电性改善的碳化物涂层,具体采用以下步骤:The method for improving the conductivity and corrosion resistance of the carbide coating on the fuel cell bipolar plate comprises depositing a metal transition layer and a metal carbide coating in sequence on the surface of the metal bipolar plate, and then engraving the coated bipolar plate Corrosion treatment to change the surface structure and composition of the carbide coating, and finally after cleaning and drying to obtain a carbide coating with improved corrosion resistance and electrical conductivity, the specific steps are as follows:

1)金属双极板预处理:将金属双极板依次置于乙醇,丙酮中,采用超声清洗并烘干;1) Metal bipolar plate pretreatment: place the metal bipolar plate in ethanol and acetone in sequence, ultrasonically clean and dry;

2)涂层制备:在金属双极板表面沉积金属过渡层及金属碳化物涂层,其中金属碳化物涂层为连续性涂层,厚度200nm,涂覆的金属碳化物为碳化铌,通过多弧离子镀制备得到;2) Coating preparation: deposit a metal transition layer and a metal carbide coating on the surface of the metal bipolar plate, wherein the metal carbide coating is a continuous coating with a thickness of 200nm, and the coated metal carbide is niobium carbide. Prepared by arc ion plating;

3)涂层刻蚀:将双极板置于刻蚀设备中进行干法刻蚀,采用的工艺气体为氯气,气体流量为10sccm,气压为10Pa,刻蚀时间为1h;3) Coating etching: the bipolar plate is placed in an etching device for dry etching, the process gas used is chlorine gas, the gas flow rate is 10 sccm, the air pressure is 10 Pa, and the etching time is 1 h;

4)取出刻蚀后的金属双极板并清洗烘干得到耐腐蚀性和导电性改善的碳化物涂层。4) Take out the etched metal bipolar plate, wash and dry to obtain a carbide coating with improved corrosion resistance and electrical conductivity.

实施例12:Example 12:

改善燃料电池双极板碳化物涂层导电及耐蚀性的方法,包括在金属双极板表面依次沉积金属过渡层和金属碳化物涂层,然后对涂覆有涂层的双极板进行刻蚀处理,改变碳化物涂层的表面结构及组成成分,最后经过清洗,烘干得到耐腐蚀性能和导电性改善的碳化物涂层,具体采用以下步骤:The method for improving the conductivity and corrosion resistance of the carbide coating on the fuel cell bipolar plate comprises depositing a metal transition layer and a metal carbide coating in sequence on the surface of the metal bipolar plate, and then engraving the coated bipolar plate Corrosion treatment to change the surface structure and composition of the carbide coating, and finally after cleaning and drying to obtain a carbide coating with improved corrosion resistance and electrical conductivity, the specific steps are as follows:

1)金属双极板预处理:将金属双极板依次置于乙醇,丙酮中,采用超声清洗并烘干;1) Metal bipolar plate pretreatment: place the metal bipolar plate in ethanol and acetone in sequence, ultrasonically clean and dry;

2)涂层制备:在金属双极板表面沉积金属过渡层及金属碳化物涂层,其中金属碳化物涂层为连续性涂层,厚度300nm,涂覆的金属碳化物为碳化钼(MoC),通过电子束蒸发制备得到;2) Coating preparation: Deposit a metal transition layer and a metal carbide coating on the surface of the metal bipolar plate, wherein the metal carbide coating is a continuous coating with a thickness of 300nm, and the coated metal carbide is molybdenum carbide (MoC) , prepared by electron beam evaporation;

3)涂层刻蚀:将双极板置于刻蚀设备中进行干法刻蚀,采用的工艺气体为四氟化碳及四氯化碳,气体流量为500sccm,气压为1000Pa,刻蚀时间为5min;3) Coating etching: place the bipolar plate in the etching equipment for dry etching, the process gas used is carbon tetrafluoride and carbon tetrachloride, the gas flow rate is 500sccm, the air pressure is 1000Pa, the etching time 5min;

4)取出刻蚀后的金属双极板并清洗烘干得到耐腐蚀性和导电性改善的碳化物涂层。4) Take out the etched metal bipolar plate, wash and dry to obtain a carbide coating with improved corrosion resistance and electrical conductivity.

以上对本发明的具体实施例进行了描述。需要理解的是,本发明并不局限于上述特定实施方式,本领域技术人员可以在权利要求的范围内做出各种变形或修改,这并不影响本发明的实质内容。Specific embodiments of the present invention have been described above. It should be understood that the present invention is not limited to the specific embodiments described above, and those skilled in the art may make various changes or modifications within the scope of the claims, which do not affect the essence of the present invention.

Claims (8)

1. improving fuel battery double plates carbide coating conduction and corrosion proof method, which is characterized in that this method is included in Metal bipolar plate surface is sequentially depositing intermediate metal and metal-carbide coating, is then carried out to coating cated bipolar plates Etching processing changes the surface texture and constituent of carbide coating, finally through over cleaning, drying obtain corrosion resistance and The carbide coating that electric conductivity improves.
2. improvement fuel battery double plates carbide coating conduction according to claim 1 and corrosion proof method, special Sign is that this method specifically uses following steps:
1) metal double polar plates pre-process:Metal double polar plates are sequentially placed into ethyl alcohol, in acetone, using being cleaned by ultrasonic and dry;
2) prepared by coating:In metal bipolar plate surface deposited metal transition zone and metal-carbide coating;
3) coating etches:Bipolar plates are completely immersed in chemical etching solution and carry out wet etching or be placed in etching apparatus to do Method etches;
4) metal double polar plates and cleaning, drying after etching are taken out and obtain the carbide coating that corrosion resistance and electric conductivity improve.
3. improvement fuel battery double plates carbide coating conduction according to claim 2 and corrosion proof method, special Sign is that the metal-carbide coating is steps coating or continuity coating, thickness 10-300nm.
4. improvement fuel battery double plates carbide coating conduction according to claim 2 and corrosion proof method, special Sign is that the metal carbides of the metal-carbide coating coating include chromium carbide (Cr3C2), titanium carbide (TiC), zirconium carbide (ZrC), one or more in niobium carbide (NbC) or molybdenum carbide (MoC).
5. improvement fuel battery double plates carbide coating conduction according to claim 2 and corrosion proof method, special Sign is that the metal-carbide coating passes through magnetron sputtering method, chemical vapor deposition, multi-arc ion coating or electron beam evaporation system It is standby to obtain.
6. improvement fuel battery double plates carbide coating conduction according to claim 2 and corrosion proof method, special Sign is that wet etching is using hydrofluoric acid solution or the mixed liquor of hydrofluoric acid and nitric acid, and etching temperature is 10-70 DEG C, etching Time is 5s-20min.
7. improvement fuel battery double plates carbide coating conduction according to claim 6 and corrosion proof method, special Sign is, the mass concentration of the hydrofluoric acid solution is 0.5%-10%, hydrofluoric acid in the mixed liquor of the hydrofluoric acid and nitric acid Mass concentration be 0.5%-10%, the mass concentration of nitric acid is 0.1%-20%.
8. improvement fuel battery double plates carbide coating conduction according to claim 2 and corrosion proof method, special Sign is, the process gas that dry etching uses include one kind in chlorine, carbon tetrafluoride, carbon tetrachloride, hydrogen or oxygen or It is several, gas flow 10-500sccm, air pressure 10-1000Pa, etch period 5min-1h.
CN201810219089.9A 2018-03-16 2018-03-16 Method for Improving Conductivity and Corrosion Resistance of Fuel Cell Bipolar Plate Carbide Coating Pending CN108574107A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
CN201810219089.9A CN108574107A (en) 2018-03-16 2018-03-16 Method for Improving Conductivity and Corrosion Resistance of Fuel Cell Bipolar Plate Carbide Coating
PCT/CN2019/070161 WO2019174373A1 (en) 2018-03-16 2019-01-03 Method for improving conductivity and corrosion resistance of fuel cell bipolar plate carbide coating

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201810219089.9A CN108574107A (en) 2018-03-16 2018-03-16 Method for Improving Conductivity and Corrosion Resistance of Fuel Cell Bipolar Plate Carbide Coating

Publications (1)

Publication Number Publication Date
CN108574107A true CN108574107A (en) 2018-09-25

Family

ID=63574269

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201810219089.9A Pending CN108574107A (en) 2018-03-16 2018-03-16 Method for Improving Conductivity and Corrosion Resistance of Fuel Cell Bipolar Plate Carbide Coating

Country Status (2)

Country Link
CN (1) CN108574107A (en)
WO (1) WO2019174373A1 (en)

Cited By (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109449457A (en) * 2018-10-31 2019-03-08 上海汉行科技有限公司 The preparation method of the metallic bipolar plate materials of proton exchange polymer membrane fuel cell
CN110247065A (en) * 2019-07-09 2019-09-17 吴同舜 A kind of fuel battery gas diffusion layer low cost continuous industrial production technique
WO2019174373A1 (en) * 2018-03-16 2019-09-19 上海交通大学 Method for improving conductivity and corrosion resistance of fuel cell bipolar plate carbide coating
CN110265668A (en) * 2019-06-19 2019-09-20 上海大学 Hydrogen fuel cell metal bipolar plate and preparation method thereof
CN110284102A (en) * 2019-06-13 2019-09-27 上海治臻新能源装备有限公司 A kind of metal carbides crystal composite coating and preparation method thereof
CN110541155A (en) * 2019-09-30 2019-12-06 上海治臻新能源装备有限公司 A four-chamber deposition system for metal carbide coatings on fuel cell plates
CN110983283A (en) * 2019-12-20 2020-04-10 欧伊翔 Preparation method and equipment of Ti/TiCN nano coating for metal bipolar plate of hydrogen fuel cell
CN111029606A (en) * 2019-12-20 2020-04-17 佛山国防科技工业技术成果产业化应用推广中心 Metal boride-based composite coating for fuel cell bipolar plate and preparation method thereof
CN111092242A (en) * 2020-02-27 2020-05-01 江苏微导纳米科技股份有限公司 A kind of preparation method of multi-nano coating structure of metal bipolar plate of proton exchange membrane fuel cell
CN111446461A (en) * 2020-03-13 2020-07-24 浙江华熔科技有限公司 A kind of preparation method of graphene coating resistant to acid medium corrosion in fuel cell
CN112582634A (en) * 2020-11-18 2021-03-30 上海治臻新能源装备有限公司 Multilayer composite carbon coating of high-corrosion-resistance fuel cell bipolar plate
CN112993298A (en) * 2019-12-14 2021-06-18 中国科学院大连化学物理研究所 Double-functional coating of fuel cell metal bipolar plate
CN112993293A (en) * 2019-12-14 2021-06-18 中国科学院大连化学物理研究所 Metal bipolar plate of fuel cell and preparation method thereof
CN113097522A (en) * 2021-03-29 2021-07-09 纳狮新材料有限公司 Bipolar plate and method for producing the same
CN113445014A (en) * 2021-07-02 2021-09-28 扬州市普锐泰新材料有限公司 Surface functional coating process for hydrogen fuel cell titanium bipolar plate
CN113921828A (en) * 2021-10-09 2022-01-11 贲道梅 Fuel cell bipolar plate and preparation method thereof
CN113953165A (en) * 2021-11-10 2022-01-21 中国航发南方工业有限公司 Spraying process of inorganic aluminum anticorrosive coating of compressor blade disc repair part and compressor blade disc
CN114843542A (en) * 2022-05-16 2022-08-02 上海交通大学内蒙古研究院 Preparation method of fuel cell metal polar plate ceramic phase low-temperature nucleation nano coating
CN115149021A (en) * 2022-08-02 2022-10-04 西部金属材料股份有限公司 Bipolar plate, preparation method thereof and application of bipolar plate in proton exchange membrane water electrolyzer or proton exchange membrane fuel cell

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114976089B (en) * 2022-05-27 2024-04-12 上海电气集团股份有限公司 Metal bipolar plate containing coating and preparation method thereof

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20020081478A1 (en) * 2000-11-24 2002-06-27 Ilona Busenbender Bipolar plate
CN1716522A (en) * 2004-06-30 2006-01-04 齐卡博制陶业有限公司 A method for the treatment of a surface of a metal-carbide substrate as well as such a metal-carbide substrate
CN1971991A (en) * 2005-11-23 2007-05-30 通用汽车环球科技运作公司 Metallic bipolar plates with high electrochemical stability and improved water management
CN101106187A (en) * 2006-07-14 2008-01-16 日产自动车株式会社 Cell electrode
CN104716339A (en) * 2015-02-03 2015-06-17 上海交通大学 Carbide and metal oxide composite coat for fuel cell metal pole plate, and production method thereof
CN106935880A (en) * 2017-03-08 2017-07-07 上海电力学院 A kind of surface modifying method of used in proton exchange membrane fuel cell aluminium alloy bipolar plates

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100386323B1 (en) * 2000-12-29 2003-06-02 남기석 Manufacturing method of bipolar plate using semiconductor materials for mini-fuel cells
EP2882019B1 (en) * 2012-07-31 2017-12-20 Nippon Steel & Sumitomo Metal Corporation Titanium or titanium alloy material for fuel cell separator having high contact conductivity with carbon and high durability, fuel cell separator including the same, and manufacturing method therefor
CN108574107A (en) * 2018-03-16 2018-09-25 上海交通大学 Method for Improving Conductivity and Corrosion Resistance of Fuel Cell Bipolar Plate Carbide Coating

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20020081478A1 (en) * 2000-11-24 2002-06-27 Ilona Busenbender Bipolar plate
CN1716522A (en) * 2004-06-30 2006-01-04 齐卡博制陶业有限公司 A method for the treatment of a surface of a metal-carbide substrate as well as such a metal-carbide substrate
CN1971991A (en) * 2005-11-23 2007-05-30 通用汽车环球科技运作公司 Metallic bipolar plates with high electrochemical stability and improved water management
CN101106187A (en) * 2006-07-14 2008-01-16 日产自动车株式会社 Cell electrode
CN104716339A (en) * 2015-02-03 2015-06-17 上海交通大学 Carbide and metal oxide composite coat for fuel cell metal pole plate, and production method thereof
CN106935880A (en) * 2017-03-08 2017-07-07 上海电力学院 A kind of surface modifying method of used in proton exchange membrane fuel cell aluminium alloy bipolar plates

Cited By (23)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2019174373A1 (en) * 2018-03-16 2019-09-19 上海交通大学 Method for improving conductivity and corrosion resistance of fuel cell bipolar plate carbide coating
CN109449457A (en) * 2018-10-31 2019-03-08 上海汉行科技有限公司 The preparation method of the metallic bipolar plate materials of proton exchange polymer membrane fuel cell
CN110284102A (en) * 2019-06-13 2019-09-27 上海治臻新能源装备有限公司 A kind of metal carbides crystal composite coating and preparation method thereof
CN110265668A (en) * 2019-06-19 2019-09-20 上海大学 Hydrogen fuel cell metal bipolar plate and preparation method thereof
CN110265668B (en) * 2019-06-19 2022-12-23 上海大学 Hydrogen fuel cell metal bipolar plate and preparation method thereof
CN110247065A (en) * 2019-07-09 2019-09-17 吴同舜 A kind of fuel battery gas diffusion layer low cost continuous industrial production technique
CN110541155A (en) * 2019-09-30 2019-12-06 上海治臻新能源装备有限公司 A four-chamber deposition system for metal carbide coatings on fuel cell plates
CN110541155B (en) * 2019-09-30 2025-01-07 上海治臻新能源股份有限公司 A four-chamber deposition system for metal carbide coatings on fuel cell plates
CN112993293A (en) * 2019-12-14 2021-06-18 中国科学院大连化学物理研究所 Metal bipolar plate of fuel cell and preparation method thereof
CN112993298A (en) * 2019-12-14 2021-06-18 中国科学院大连化学物理研究所 Double-functional coating of fuel cell metal bipolar plate
CN110983283A (en) * 2019-12-20 2020-04-10 欧伊翔 Preparation method and equipment of Ti/TiCN nano coating for metal bipolar plate of hydrogen fuel cell
CN111029606A (en) * 2019-12-20 2020-04-17 佛山国防科技工业技术成果产业化应用推广中心 Metal boride-based composite coating for fuel cell bipolar plate and preparation method thereof
CN111092242A (en) * 2020-02-27 2020-05-01 江苏微导纳米科技股份有限公司 A kind of preparation method of multi-nano coating structure of metal bipolar plate of proton exchange membrane fuel cell
CN111446461B (en) * 2020-03-13 2021-05-28 浙江华熔科技有限公司 A kind of preparation method of graphene coating resistant to acid medium corrosion in fuel cell
CN111446461A (en) * 2020-03-13 2020-07-24 浙江华熔科技有限公司 A kind of preparation method of graphene coating resistant to acid medium corrosion in fuel cell
CN112582634A (en) * 2020-11-18 2021-03-30 上海治臻新能源装备有限公司 Multilayer composite carbon coating of high-corrosion-resistance fuel cell bipolar plate
CN113097522A (en) * 2021-03-29 2021-07-09 纳狮新材料有限公司 Bipolar plate and method for producing the same
CN113445014A (en) * 2021-07-02 2021-09-28 扬州市普锐泰新材料有限公司 Surface functional coating process for hydrogen fuel cell titanium bipolar plate
CN113921828A (en) * 2021-10-09 2022-01-11 贲道梅 Fuel cell bipolar plate and preparation method thereof
CN113953165A (en) * 2021-11-10 2022-01-21 中国航发南方工业有限公司 Spraying process of inorganic aluminum anticorrosive coating of compressor blade disc repair part and compressor blade disc
CN114843542A (en) * 2022-05-16 2022-08-02 上海交通大学内蒙古研究院 Preparation method of fuel cell metal polar plate ceramic phase low-temperature nucleation nano coating
CN114843542B (en) * 2022-05-16 2024-01-02 上海交通大学内蒙古研究院 Preparation method of ceramic phase low-temperature nucleation nano-coating of metal polar plate of fuel cell
CN115149021A (en) * 2022-08-02 2022-10-04 西部金属材料股份有限公司 Bipolar plate, preparation method thereof and application of bipolar plate in proton exchange membrane water electrolyzer or proton exchange membrane fuel cell

Also Published As

Publication number Publication date
WO2019174373A1 (en) 2019-09-19

Similar Documents

Publication Publication Date Title
CN108574107A (en) Method for Improving Conductivity and Corrosion Resistance of Fuel Cell Bipolar Plate Carbide Coating
CN110684946B (en) Metal bipolar plate high-conductivity corrosion-resistant protective coating and preparation method and application thereof
CN106374116B (en) High-entropy alloy composite coating and process on metal bipolar plate of fuel cell
US6864007B1 (en) Corrosion resistant coated fuel cell plate with graphite protective barrier and method of making the same
CN106129422B (en) Improve the densification of fuel battery metal double polar plate overlay coating and corrosion resistant method
CN108390075A (en) Anticorrosive conductive film and its pulsed bias replace magnetron sputtering deposition methods and applications
CN113265638B (en) High-conductivity corrosion-resistant graphite-like carbon protective multilayer composite coating and preparation method and application thereof
CN106252682A (en) Fuel battery metal pole plate multiple phase coating of suppression column crystal and preparation method thereof
CN108060398A (en) A kind of fuel cell composite Nano coating and its plating method
CN112993298A (en) Double-functional coating of fuel cell metal bipolar plate
CN114481048B (en) High-conductivity corrosion-resistant amorphous/nanocrystalline composite coexisting coating and preparation method and application thereof
CN113249683A (en) MAX phase solid solution composite coating with high conductivity, corrosion resistance and long service life, and preparation method and application thereof
CN108018529A (en) Aluminum-based fuel cell bipolar plate surface composite coating and preparation method thereof
CN114597436A (en) A kind of protective coating for metal bipolar plate and preparation method thereof
CN115029663A (en) Metal polar plate composite coating, metal polar plate and preparation method thereof, and fuel cell
CN115832336B (en) Fuel cell metal polar plate precoat and preparation method thereof
CN107881466B (en) Silver-doped graphite-like carbon coating and preparation method thereof
CN114023986B (en) Composite coating for fuel cell titanium substrate bipolar plate and preparation method thereof
CN111600043A (en) Fuel cell metal bipolar plate and surface coating method thereof
CN106673050B (en) A kind of preparation method of three-dimensional dendritic nano-CuO
CN114843542B (en) Preparation method of ceramic phase low-temperature nucleation nano-coating of metal polar plate of fuel cell
CN116936786A (en) Preparation method of graphene modified aluminum foil
CN114540752B (en) Fuel cell metal plate with conductive corrosion-resistant coating and preparation method thereof
CN119372709B (en) Method for preparing oxygen evolution electrode
CN119372708B (en) A hydrogen evolution electrode for cathode of AEM electrolytic cell and preparation method thereof

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication

Application publication date: 20180925

RJ01 Rejection of invention patent application after publication