CN107342425A - The preparation of bifunctional catalyst diatomite confinement cobalt platinum based composites and its application in electrocatalytic oxidation reduction and oxygen evolution reaction - Google Patents

The preparation of bifunctional catalyst diatomite confinement cobalt platinum based composites and its application in electrocatalytic oxidation reduction and oxygen evolution reaction Download PDF

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CN107342425A
CN107342425A CN201710541669.5A CN201710541669A CN107342425A CN 107342425 A CN107342425 A CN 107342425A CN 201710541669 A CN201710541669 A CN 201710541669A CN 107342425 A CN107342425 A CN 107342425A
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diatomite
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唐正华
王凯
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South China University of Technology SCUT
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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/86Inert electrodes with catalytic activity, e.g. for fuel cells
    • H01M4/88Processes of manufacture
    • H01M4/8825Methods for deposition of the catalytic active composition
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M12/00Hybrid cells; Manufacture thereof
    • H01M12/04Hybrid cells; Manufacture thereof composed of a half-cell of the fuel-cell type and of a half-cell of the primary-cell type
    • H01M12/06Hybrid cells; Manufacture thereof composed of a half-cell of the fuel-cell type and of a half-cell of the primary-cell type with one metallic and one gaseous electrode
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/86Inert electrodes with catalytic activity, e.g. for fuel cells
    • H01M4/90Selection of catalytic material
    • H01M4/9041Metals or alloys
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/86Inert electrodes with catalytic activity, e.g. for fuel cells
    • H01M4/90Selection of catalytic material
    • H01M4/92Metals of platinum group
    • H01M4/921Alloys or mixtures with metallic elements

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Abstract

本发明公开了一种通过简易方法制备的硅藻土(DTM)限域钴铂基复合材料(CoPt‑x/DTM‑C)的制备及其电催化应用。该发明的优势在于:(1)制备方法简单:首先利用DTM的孔道吸附Pt4+和Co2+离子,然后将Pt4+和Co2+离子还原,用该方法制备的催化剂在反应中结构不易破坏;(2)催化活性高:氧还原反应中,复合材料的质量活性和比活度分别是CoPt‑x/C的2.5和1.5倍,是铂碳的4.6和2.2倍。在析氧反应中,CoPt‑x/DTM‑C的过电势相比CoPt‑x/C减小了30mV;(3)成本低廉:该催化剂Pt含量低,硅藻土来源广泛,极大地降低了催化剂的成本,具有良好的商业化应用前景。

The invention discloses the preparation of a diatomite (DTM) confined cobalt-platinum-based composite material (CoPt-x/DTM-C) prepared by a simple method and its electrocatalytic application. The advantages of this invention are: (1) The preparation method is simple: firstly, the pores of DTM are used to adsorb Pt 4+ and Co 2+ ions, and then the Pt 4+ and Co 2+ ions are reduced. (2) High catalytic activity: In the oxygen reduction reaction, the mass activity and specific activity of the composite are 2.5 and 1.5 times that of CoPt‑x/C, and 4.6 and 2.2 times that of platinum carbon. In the oxygen evolution reaction, the overpotential of CoPt‑x/DTM‑C is 30mV lower than that of CoPt‑x/C; (3) Low cost: the catalyst has a low Pt content and a wide range of sources of diatomite, which greatly reduces the The cost of the catalyst has good prospects for commercial application.

Description

双功能催化剂硅藻土限域钴铂基复合材料的制备及其在电催 化氧还原和析氧反应中的应用Preparation of diatomite-confined cobalt-platinum-based composites as bifunctional catalysts and their application in electrocatalysis Applications in Oxygen Reduction and Oxygen Evolution Reactions

技术领域technical field

本发明制备的限域钴铂合金纳米材料应用于电催化氧还原和析氧反应,属于新能源材料领域。具体涉及到纳米催化剂的制备,以及在金属-空气电池和质子交换膜燃料电池中的应用。The confined cobalt-platinum alloy nanomaterial prepared by the invention is applied to electrocatalytic oxygen reduction and oxygen evolution reaction, and belongs to the field of new energy materials. It specifically relates to the preparation of nano-catalysts and their applications in metal-air batteries and proton exchange membrane fuel cells.

背景技术Background technique

新型能量转换和存储设备是解决当前能源与环境问题的有效途径,燃料电池具有能量转化效率高,环境友好,携带方便等特点受到社会的广泛关注。质子交换膜燃料电池具有清洁无污染、工作温度低、启动快、结构简单及操作方便等优点,既可应用于大型发电厂,也可应用于人们日常生活中的手机、笔记本电脑和电动汽车等电源设备。其阳极发生氢燃料的氧化,阴极发生氧气的还原,两极都含有加速电极电化学反应的催化剂,然而阴极反应速率低,是制约燃料电池商业化发展的主要瓶颈。目前阴极氧还原催化剂主要是铂基贵金属材料,然而其活性和稳定性都不能满足燃料电池发展的需要,此外铂为贵金属,地壳含量有限,成本也很高。因此提高铂基催化剂的活性和稳定性,降低铂的使用量,是研究阴极氧还原催化剂的主要方向。金属空气电池是燃料电池的一种,其反应方程为;负极:M-xe-=Mx +;正极:O2-xe-=x/2O2- (方程1)New energy conversion and storage devices are an effective way to solve current energy and environmental problems. Fuel cells have attracted widespread attention from society for their high energy conversion efficiency, environmental friendliness, and portability. Proton exchange membrane fuel cells have the advantages of clean and pollution-free, low working temperature, fast start-up, simple structure and convenient operation. power supply. The oxidation of hydrogen fuel occurs at the anode, and the reduction of oxygen occurs at the cathode. Both electrodes contain catalysts that accelerate the electrochemical reaction of the electrodes. However, the low reaction rate of the cathode is the main bottleneck restricting the commercial development of fuel cells. At present, the cathodic oxygen reduction catalyst is mainly based on platinum-based noble metal materials, but its activity and stability cannot meet the needs of fuel cell development. In addition, platinum is a noble metal with limited earth crust content and high cost. Therefore, improving the activity and stability of platinum-based catalysts and reducing the amount of platinum used are the main directions of research on cathode oxygen reduction catalysts. A metal-air battery is a type of fuel cell, and its reaction equation is: Negative pole: M-xe - = M x + ; Positive pole: O 2 -xe - = x/2O 2- (equation 1)

由反应方程(1)可知,金属空气电池负极金属失去电子,正极上O2得到电子。负极材料一般为金属Zn、Al等地壳含量高的元素,众所周知,Zn、Al金属单质的制备技术已经成熟,而且Zn、Al等金属在电解液很容易失去电子,因此负极材料不是制约金属空气电池发展的主要因素。相反,正极端O2的还原要比Zn、Al金属的氧化困难很多,需要有催化剂辅助,而且O2在电解液中的浓度越高,电池的性能就越优。这就要求负极材料具备两个基本性能:(1)催化氧气还原的性能;(2)催化电解液产氧的性能。目前的金属-空气电池正极材料价格昂贵,制造工艺繁琐,催化稳定性差,制约了金属-空气电池的商业化发展。所以,廉价、高效以及制备工艺简单的双功能催化剂是推进金属空气电池进一步发展的关键。It can be seen from the reaction equation (1) that the metal at the negative electrode of the metal-air battery loses electrons, and O2 on the positive electrode gains electrons. Anode materials are generally elements with high crustal content such as metal Zn and Al. As we all know, the preparation technology of Zn and Al metal elements is mature, and metals such as Zn and Al are easy to lose electrons in the electrolyte, so the anode material is not a constraint for metal-air batteries. main factor of development. On the contrary, the reduction of O2 at the positive end is much more difficult than the oxidation of Zn and Al metals, and requires the assistance of a catalyst, and the higher the concentration of O2 in the electrolyte, the better the performance of the battery. This requires the anode material to have two basic properties: (1) the performance of catalyzing the reduction of oxygen; (2) the performance of catalyzing the oxygen production of the electrolyte. The current metal-air battery cathode materials are expensive, the manufacturing process is cumbersome, and the catalytic stability is poor, which restricts the commercial development of metal-air batteries. Therefore, cheap, efficient and simple preparation process of bifunctional catalysts is the key to promote the further development of metal-air batteries.

Pt基贵金属与过渡金属M(M=Fe、Co、Ni、Mn、Cu等)组成的合金纳米材料在氧还原性能方面有了很大的改进,然而其性能衰减太快,影响了燃料电池的商业化使用。采用硅藻土限域的合金纳米粒子可以在一定程度上抑制了催化剂活性的衰减,提升了催化剂的长期稳定性。Alloy nanomaterials composed of Pt-based noble metals and transition metals M (M=Fe, Co, Ni, Mn, Cu, etc.) have greatly improved oxygen reduction performance, but their performance decays too fast, which affects the performance of fuel cells. commercial use. The use of diatomite-confined alloy nanoparticles can inhibit the attenuation of catalyst activity to a certain extent and improve the long-term stability of the catalyst.

析氧催化剂目前以RuO2和IrO2贵金属氧化物和Fe、Co、Ni等过渡金属氧化物以及过渡金属氢氧化物和碳材料为主,然而RuO2和IrO2贵金属氧化物价格昂贵且稳定性差,过渡金属氧化物及氢氧化物和碳材料虽然降低了成本,但是其性能和稳定性还是不能满足金属-空气电池发展的需要。PtCo-x/DTM-C具有良好的氧还原和析氧催化活性,而且Pt含量低,DTM资源丰富,成本低廉,在金属-空气电池的发展方面具有良好的应用前景。Oxygen evolution catalysts are currently dominated by noble metal oxides such as RuO 2 and IrO 2 , transition metal oxides such as Fe, Co, and Ni, transition metal hydroxides, and carbon materials, but RuO 2 and IrO 2 noble metal oxides are expensive and have poor stability Although transition metal oxides and hydroxides and carbon materials have reduced costs, their performance and stability still cannot meet the needs of the development of metal-air batteries. PtCo-x/DTM-C has good catalytic activity for oxygen reduction and oxygen evolution, and low Pt content, abundant DTM resources, low cost, and has good application prospects in the development of metal-air batteries.

燃料电池阴极催化剂一般是铂基贵金属材料,该催化剂制造成本高而且使用量大。因此阴极催化剂的成本是燃料电池价格高昂主要因素。PtCo-x/DTM-C催化剂Pt含量低、采用了硅藻土对金属纳米粒子的限域保护,其活性和稳定性有了改善,而且合成条件温和方法简单,具有工业化生产的前景。Fuel cell cathode catalysts are generally platinum-based noble metal materials, which are expensive to manufacture and used in large quantities. Therefore, the cost of the cathode catalyst is a major factor in the high price of fuel cells. The PtCo-x/DTM-C catalyst has a low Pt content and uses diatomite to confine metal nanoparticles. Its activity and stability have been improved, and the synthesis conditions are mild and the method is simple, which has the prospect of industrial production.

本发明采用双功能催化剂硅藻土限域钴铂基复合材料的制备及其在电催化氧还原和析氧反应中的应用,尚未有公开的文献或专利报道。The preparation of the diatomite-confined cobalt-platinum-based composite material used in the present invention and its application in electrocatalytic oxygen reduction and oxygen evolution reactions have not yet been published in literature or patent reports.

发明内容Contents of the invention

双功能催化剂硅藻土限域钴铂基复合材料的制备方法,并将其用于电催化氧还原和析氧反应中。The preparation method of diatomite-confined cobalt-platinum-based composite material as a bifunctional catalyst is used in electrocatalytic oxygen reduction and oxygen evolution reactions.

本发明是通过以下技术方案实现的,具体包括以下几个步骤:The present invention is achieved through the following technical solutions, specifically comprising the following steps:

(1)将硅藻土分散到40mL 3mol L-1的HCl溶液中,充分搅拌12h,然后抽滤,用去离子水洗涤至滤液pH~7,将滤饼在真空烘箱中50℃干燥,产物标记为DTM备用。(1) Disperse diatomaceous earth into 40mL of 3mol L -1 HCl solution, stir well for 12h, then suction filter, wash with deionized water until the filtrate pH ~ 7, dry the filter cake in a vacuum oven at 50°C, the product Marked as DTM spare.

(2)控制Co和Pt的摩尔比为Co/Pt=1、Co/Pt=3和Co/Pt=9,将Co和Pt的前驱体盐CoCl2·6H2O和H2PtCl6·6H2O添加到20mL EG溶液中,待前驱体盐完全溶解后加入76mg DTM,磁力搅拌30min后,开始从室温加热到160℃保持6h。(2) Control the molar ratio of Co and Pt to be Co/Pt=1, Co/Pt=3 and Co/Pt=9, and the precursor salts of Co and Pt CoCl 2 ·6H 2 O and H 2 PtCl 6 ·6H 2 O was added to 20mL EG solution, after the precursor salt was completely dissolved, 76mg DTM was added, and after magnetic stirring for 30min, it was heated from room temperature to 160°C for 6h.

(3)在反应温度下降到40℃时加入76mg碳粉,磁力搅拌4h,离心洗涤,真空条件下50℃干燥12h。(3) When the reaction temperature dropped to 40°C, 76 mg of carbon powder was added, magnetically stirred for 4 hours, washed by centrifugation, and dried at 50°C under vacuum for 12 hours.

(4)取所制备的催化剂涂敷在玻碳工作电极上,其载量为80.8ug cm-2,氧还原测试条件为氧气饱和的0.1mol L-1KOH电解液中在旋转条件下测试,析氧反应为N2饱和的1molL-1KOH溶液,测试温度为室温。(4) The prepared catalyst was coated on a glassy carbon working electrode with a loading capacity of 80.8ug cm -2 , and the oxygen reduction test condition was tested under rotating conditions in an oxygen-saturated 0.1mol L -1 KOH electrolyte, The oxygen evolution reaction is a 1molL -1 KOH solution saturated with N 2 , and the test temperature is room temperature.

步骤(1)所使用的DTM是为了限域CoPt纳米粒子,抑制纳米粒子在反应中出现团聚现象,从而保持催化剂的活性。The DTM used in the step (1) is to confine the CoPt nanoparticles and inhibit the agglomeration of the nanoparticles during the reaction, thereby maintaining the activity of the catalyst.

步骤(2)所使用的EG为还原剂和溶剂,在温度为160℃时可还原Pt+4和Co+2,还可将Pt+4和Co+2扩散到DTM的孔道当中。The EG used in step (2) is a reducing agent and a solvent, which can reduce Pt +4 and Co +2 at a temperature of 160°C, and can also diffuse Pt +4 and Co +2 into the pores of DTM.

步骤(3)所加的碳粉是为了保护硅藻土,使其在反应中不易被电解液刻蚀,碳粉还可促进电荷在催化剂材料上的传递速率,增强了催化剂CoPt与催化底物间的电荷传递。The carbon powder added in step (3) is to protect the diatomite so that it is not easy to be etched by the electrolyte during the reaction. The carbon powder can also promote the transfer rate of the charge on the catalyst material, and strengthen the catalyst CoPt and the catalytic substrate. charge transfer between them.

步骤(4)采用旋转圆盘电极是为了加快O2在电极上的扩散,更真实地表征材料本身的催化性能。The purpose of using the rotating disk electrode in step (4) is to speed up the diffusion of O2 on the electrode and to characterize the catalytic performance of the material itself more truly.

综上所述,与现有的技术相比,本发明的优异之处在于:In summary, compared with the prior art, the present invention is superior in that:

(1)本发明的制备方法简单,不需要煅烧,避免了因煅烧而产生的污染和能源消耗,既环保又节能,简化了合成工艺。(1) The preparation method of the present invention is simple, does not require calcination, avoids pollution and energy consumption caused by calcination, is environmentally friendly and energy-saving, and simplifies the synthesis process.

(2)合成的CoPt-x/DTM-C催化剂,CoPt纳米催化剂被限域在DTM孔道当中,在氧还原和产氧过程中具有较大的催化活性,耐受性也得到了显著提高。(2) The synthesized CoPt-x/DTM-C catalyst, the CoPt nano-catalyst is confined in the DTM channel, has greater catalytic activity in the process of oxygen reduction and oxygen generation, and the tolerance has also been significantly improved.

(3)该方法合成的催化剂在氧还原反应中其起始电位和半波电位均优于商业Pt/C,极限电流密度、电子转移数和H2O2产率也与商业Pt/C媲美,稳定性也远超商业Pt/C,为燃料电池与金属-空气电池提供了一种高效的双功能催化剂,具有良好的应用前景。( 3 ) The onset potential and half - wave potential of the catalyst synthesized by this method are superior to commercial Pt/C in the oxygen reduction reaction, and the limiting current density, electron transfer number and H2O2 yield are also comparable to commercial Pt/C , and the stability is far superior to that of commercial Pt/C, which provides an efficient dual-function catalyst for fuel cells and metal-air batteries, and has good application prospects.

附图说明Description of drawings

图1a、b和c分别为CoPt-9/DTM-C催化剂不同放大倍数的透射电镜(TEM)分析。Figure 1a, b, and c are the transmission electron microscopy (TEM) analyzes of the CoPt-9/DTM-C catalyst at different magnifications, respectively.

图2为CoPt-9/DTM-C和CoPt-9/C的X-射线衍射图谱。Figure 2 is the X-ray diffraction patterns of CoPt-9/DTM-C and CoPt-9/C.

图3和图4分别为DTM和CoPt-9/DTM-C的氮气吸脱附等温曲线图谱,其中插入图为相应的孔径分布。Figure 3 and Figure 4 are the nitrogen adsorption-desorption isotherm profiles of DTM and CoPt-9/DTM-C, respectively, and the inserts are the corresponding pore size distributions.

图5为CoPt-9/DTM-C和CoPt-9/C的X-射线光电子衍射图谱。Figure 5 is the X-ray photoelectron diffraction patterns of CoPt-9/DTM-C and CoPt-9/C.

图6为CoPt-1/DTM-C、CoPt-3/DTM-C和CoPt-9/DTM-C和Pt/DTM-C在O2饱和的0.1mol L-1KOH溶液中的极化曲线图谱。Figure 6 shows the polarization curves of CoPt-1/DTM-C, CoPt-3/DTM-C, CoPt-9/DTM-C and Pt/DTM-C in O2 saturated 0.1mol L -1 KOH solution .

图7为CoPt-1/DTM-C、CoPt-1/C和Pt/C在O2饱和的0.1mol L-1KOH溶液中的极化曲线图谱。Figure 7 shows the polarization curves of CoPt-1/DTM-C, CoPt-1/C and Pt/C in O 2 saturated 0.1mol L -1 KOH solution.

图8为CoPt-1/DTM-C电极以不同旋转速度在O2饱和的0.1mol L-1KOH溶液中的极化曲线图谱。Figure 8 shows the polarization curves of the CoPt-1/DTM-C electrode in O2 -saturated 0.1mol L -1 KOH solution at different rotation speeds.

图9为CoPt-1/DTM-C在O2饱和的0.1mol L-1KOH溶液中催化氧气还原时的电子转移数和双氧水产率。Figure 9 shows the number of electrons transferred and the yield of hydrogen peroxide when CoPt-1/DTM-C catalyzes oxygen reduction in O 2 -saturated 0.1 mol L -1 KOH solution.

图10为CoPt-9/DTM-C和CoPt-9/C在氮气饱和的1mol L-1KOH溶液中的极化曲线。Figure 10 shows the polarization curves of CoPt-9/DTM-C and CoPt-9/C in nitrogen-saturated 1mol L -1 KOH solution.

图11为CoPt-9/DTM-C、CoPt-9/C、Co/DTM-C和Co/C的塔菲尔曲线及其斜率。Fig. 11 shows the Tafel curves and their slopes of CoPt-9/DTM-C, CoPt-9/C, Co/DTM-C and Co/C.

图12为CoPt-1/DTM-C和CoPt-1/C的氧还原稳定性对比。Figure 12 is a comparison of the oxygen reduction stability of CoPt-1/DTM-C and CoPt-1/C.

图13为CoPt-9/DTM-C和CoPt-9/-C的析氧稳定性对比。Figure 13 is a comparison of the oxygen evolution stability of CoPt-9/DTM-C and CoPt-9/-C.

具体实施方式detailed description

下面结合实例对本发明进一步说明,但本发明并不限于以下实施例。Below in conjunction with example the present invention is further described, but the present invention is not limited to following examples.

实施例1。Example 1.

(1)将硅藻土分散到40mL 3mol L-1的HCl溶液中,磁力搅拌12h,然后抽滤,用去离子水洗涤至滤液pH~7,将滤饼在真空烘箱中50℃干燥12h,产物标记为DTM备用。(1) Disperse diatomaceous earth into 40 mL of 3 mol L -1 HCl solution, stir magnetically for 12 h, then suction filter, wash with deionized water until the filtrate pH ~ 7, and dry the filter cake in a vacuum oven at 50 ° C for 12 h, The product is marked as DTM for future use.

(2)控制Co和Pt的摩尔比为Co/Pt=1将Co和Pt的前驱体盐0.25mmol CoCl2·6H2O和0.25mol H2PtCl6·6H2O,添加到20mL EG溶液中,待前驱体盐完全溶解后加入76mg DTM,搅拌一定30min后,开始从室温加热到160℃保持6h。(2) Control the molar ratio of Co and Pt to Co/Pt=1, add the precursor salt of Co and Pt 0.25mmol CoCl 2 ·6H 2 O and 0.25mol H 2 PtCl 6 ·6H 2 O to 20mL EG solution After the precursor salt is completely dissolved, add 76mg of DTM, stir for 30min, then start heating from room temperature to 160°C for 6h.

(3)在反应温度下降到40℃时加入76mg碳粉,搅拌一4h,离心洗涤。真空条件下50℃干燥12h即可得到CoPt-1/DTM-C催化剂。(3) When the reaction temperature drops to 40°C, add 76 mg of carbon powder, stir for 4 hours, and wash by centrifugation. CoPt-1/DTM-C catalyst can be obtained by drying at 50℃ for 12h under vacuum condition.

电化学性能测试:Electrochemical performance test:

电化学测试表征是在上海辰华公司生产的CHI 750E电化学工作站,采用三电极体系进行测试,铂片为对电极,Ag/AgCl电极为参比电极,负载有催化剂的玻璃碳电极为工作电极。称取2mg催化剂于1.0mL乙醇溶液中,滴加10μL Nafion配置标准溶液,将混合液超声30分钟,得浓度为2mg/mL的催化剂悬浮液。取10μL催化剂悬浮液均匀涂抹在玻碳电极上并在空气中自然干燥,得到催化剂负载量为80.8μg/cm2。氧还原性能测试时将工作电极置于氧饱和的0.1M KOH溶液中进行伏安循环特性测试,析氧性能测试是在N2饱和的1M KOH溶液中进行。结构和性能表征如图所示。The electrochemical test and characterization was performed on the CHI 750E electrochemical workstation produced by Shanghai Chenhua Company. The three-electrode system was used for testing. The platinum sheet was used as the counter electrode, the Ag/AgCl electrode was used as the reference electrode, and the glassy carbon electrode loaded with catalyst was used as the working electrode. . Weigh 2 mg of the catalyst into 1.0 mL of ethanol solution, add 10 μL of Nafion dropwise to prepare a standard solution, and sonicate the mixture for 30 minutes to obtain a catalyst suspension with a concentration of 2 mg/mL. 10 μL of the catalyst suspension was evenly spread on the glassy carbon electrode and dried naturally in the air to obtain a catalyst loading of 80.8 μg/cm 2 . During the oxygen reduction performance test, the working electrode was placed in an oxygen-saturated 0.1M KOH solution for the voltammetric cycle characteristic test, and the oxygen evolution performance test was carried out in a N 2 saturated 1M KOH solution. The structure and performance characterization are shown in the figure.

图1透射电镜可以看出CoPt合金纳米粒子附着在硅藻土和碳载体上,高放大倍数图(c)表明纳米粒子存在两种不同的晶格条纹,其间距分别是 分别代表PtCo合金的(111)晶面和(200)晶面,这与图2的X-射线衍射图谱相对应。图2中可以观察到加入硅藻土前后CoPt合金的晶型未发生变化,分别都在2theta为40.1°、46.2°和68.2°处出现了CoPt的(111)、(200)和(220)晶面,说明CoPt合金纳米粒子为面型立方(FCC)结构。同时在21.9°也出现了硅藻土的非晶态衍射峰。Figure 1 Transmission electron microscope shows that CoPt alloy nanoparticles are attached to diatomaceous earth and carbon support. The high magnification image (c) shows that there are two different lattice fringes in the nanoparticles, and the distances are with Represent the (111) crystal plane and (200) crystal plane of the PtCo alloy, respectively, which correspond to the X-ray diffraction pattern in Figure 2. It can be observed in Figure 2 that the crystal form of the CoPt alloy does not change before and after adding diatomite, and the (111), (200) and (220) crystals of CoPt appear at 2theta of 40.1°, 46.2° and 68.2° respectively. On the surface, it shows that the CoPt alloy nanoparticles have a face cubic (FCC) structure. At the same time, the amorphous diffraction peak of diatomite also appeared at 21.9°.

图3和图4的N2-吸脱附等温曲线图表明,DTM和CoPt-9/DTM-C的曲线属于典型的IV型曲线,插入图可以看出,硅藻土的孔径分布在10-30nm之间,10nm以内的孔径也有分布,而加入CoPt和碳粉后孔径主要分布在6nm左右和13nm左右,所以CoPt纳米粒子和碳粉减小了硅藻土的孔径。证明纳米粒子可以在硅藻土内合成,而且XC-72颗粒也可以很好地填充到孔道当中,从而增加CoPt合金与催化底物的电子传输能力。The N2 -adsorption-desorption isotherm graphs in Fig. 3 and Fig. 4 show that the curves of DTM and CoPt-9/DTM-C belong to the typical IV-type curves, and it can be seen from the insert that the pore size distribution of diatomite is between 10- Between 30nm and within 10nm, the pore size also has a distribution, and after adding CoPt and carbon powder, the pore size is mainly distributed around 6nm and 13nm, so CoPt nanoparticles and carbon powder reduce the pore size of diatomite. It is proved that nanoparticles can be synthesized in diatomaceous earth, and XC-72 particles can also be well filled into the pores, thereby increasing the electron transport ability of CoPt alloy and catalytic substrate.

图5X-射线光电子衍射表明硅藻土的加入改变了CoPt的结合能,由图可以看出当加入硅藻土以后Pt 4f7/2的结合能正移14eV,已有研究表明费米能级也会随着结合能降低,费米能级的降低会弱化化学吸附键能,使得吸附在CoPt表面的含氧物质,在CoPt的催化作用下含氧的键更易断裂,从而促进了材料对氧的催化性能。Figure 5 X-ray photoelectron diffraction shows that the addition of diatomaceous earth changes the binding energy of CoPt. It can be seen from the figure that the binding energy of Pt 4f 7/2 shifts positively by 14eV when diatomite is added. Studies have shown that the Fermi level With the reduction of binding energy, the reduction of Fermi energy level will weaken the chemical adsorption bond energy, so that the oxygen-containing species adsorbed on the surface of CoPt will be more easily broken under the catalysis of CoPt, thus promoting the material to oxygen. catalytic performance.

图6为氧还原反应的极化曲线,负载有本实施例制备的催化剂随着Co含量的增加,起始电位逐渐负移,由图可知CoPt-1起始电位为1.0V左右,而CoPt-9在0.95V左右。Figure 6 is the polarization curve of the oxygen reduction reaction. With the catalyst prepared in this example, the initial potential gradually shifts negatively with the increase of Co content. It can be seen from the figure that the initial potential of CoPt-1 is about 1.0V, while that of CoPt- 9 at around 0.95V.

图7显示CoPt-1/C催化剂起始电位为0.94V,较CoPt-1/DTM-C过电位增加了40mV左右,而且CoPt-1/DTM-C的过电位比Pt/C小10mV左右。Pt/C在电压0.4V(vs.RHE)时的电流密度为4.8mA cm-2,而CoPt-1/DTM-C在相同电压下的电流密度达到5.4mA cm-2,CoPt-1/C的为4.7mA cm-2。说明硅藻土的加入不仅促进了材料的起始电位而且增加了极限扩散电流。Figure 7 shows that the onset potential of CoPt-1/C catalyst is 0.94V, which is about 40mV higher than that of CoPt-1/DTM-C, and the overpotential of CoPt-1/DTM-C is about 10mV lower than that of Pt/C. The current density of Pt/C at 0.4V (vs.RHE) is 4.8mA cm -2 , while the current density of CoPt-1/DTM-C reaches 5.4mA cm -2 at the same voltage, and CoPt-1/C is 4.7mA cm -2 . It shows that the addition of diatomite not only promotes the initial potential of the material but also increases the limiting diffusion current.

图8为CoPt-1/DTM-C氧还原性能相应的K-L曲线,由图可知不同旋转速率下的电流表现出良好的线性关系,说明该反应是理想的一级反应过程。Figure 8 is the K-L curve corresponding to the oxygen reduction performance of CoPt-1/DTM-C. It can be seen from the figure that the current at different rotation rates shows a good linear relationship, indicating that the reaction is an ideal first-order reaction process.

图9为CoPt-1/DTM-C催化氧气还原反应时的电子转移数和副产物双氧水的产率,由图可以看出加入硅藻土后电子转移数由3.85提高到3.92,双氧水的产率也从平均5.5%降到4.5%左右。Figure 9 shows the number of electron transfers and the yield of by-product hydrogen peroxide when CoPt-1/DTM-C catalyzes the oxygen reduction reaction. It can be seen from the figure that the number of electron transfers increases from 3.85 to 3.92 after adding diatomaceous earth, and the yield of hydrogen peroxide It also dropped from an average of 5.5% to around 4.5%.

本实施例所制备的催化剂在析氧反应中的性能曲线如图10所示,CoPt-9/DTM-C在电流密度10mA cm-2时的过电位为380mV而CoPt-9/C是410mV,硅藻土的加入将CoPt-9催化剂的过电位减少了30mV左右,Co/DTM-C的过电位也比Co/C减少了25mV左右,因此硅藻土也提高了催化剂的析氧性能。Tafel曲线对CoPt-9/DTM-C、CoPt-9/C、Co/DTM-C和Co/C的动力学性能做了表征,由图11可以看出相应的斜率为120mV dec-1、136mV dec-1、132mV dec-1和137mVdec-1,其中CoPt-1/DTM-C的斜率比CoPt-1/C低16mV dec-1,Co/DTM-C也Co/C的低5mV dec-1,说明硅藻土的加入从动力上促进了材料的催化性能。The performance curve of the catalyst prepared in this example in the oxygen evolution reaction is shown in Figure 10, the overpotential of CoPt-9/DTM-C at a current density of 10mA cm -2 is 380mV and that of CoPt-9/C is 410mV, The addition of diatomaceous earth reduces the overpotential of CoPt-9 catalyst by about 30mV, and the overpotential of Co/DTM-C is also reduced by about 25mV compared with Co/C, so diatomite also improves the oxygen evolution performance of the catalyst. The Tafel curves characterize the kinetic properties of CoPt-9/DTM-C, CoPt-9/C, Co/DTM-C and Co/C. It can be seen from Figure 11 that the corresponding slopes are 120mV dec -1 , 136mV dec -1 , 132mV dec -1 and 137mVdec -1 , where the slope of CoPt-1/DTM-C is 16mV dec -1 lower than that of CoPt-1/C, Co/DTM-C is also 5mV dec -1 lower than that of Co/C , indicating that the addition of diatomite promotes the catalytic performance of the material dynamically.

图12和图13为相应的稳定性测试,由图可知,加入硅藻土后材料的氧还原稳定性从CoPt-1/C的81%增加到CoPt-1/DTM-C的95%,析氧稳定性由CoPt-9/C的81.6%增加到CoPt-9/DTM-C的93.4%。这些结果证明了硅藻土在催化反应过程中确实起到了保护CoPt纳米粒子,增强催化剂长期稳定性的作用。Figure 12 and Figure 13 are the corresponding stability tests. It can be seen from the figure that the oxygen reduction stability of the material increases from 81% of CoPt-1/C to 95% of CoPt-1/DTM-C after adding diatomaceous earth. The oxygen stability increased from 81.6% of CoPt-9/C to 93.4% of CoPt-9/DTM-C. These results prove that diatomaceous earth does protect the CoPt nanoparticles during the catalytic reaction and enhance the long-term stability of the catalyst.

实施例2。Example 2.

(1)将硅藻土分散到40mL 3mol L-1的HCl溶液中,磁力搅拌12h,然后抽滤,用去离子水洗涤至滤液pH~7,将滤饼在真空烘箱中50℃干燥12h,产物标记为DTM备用。(1) Disperse diatomaceous earth into 40 mL of 3 mol L -1 HCl solution, stir magnetically for 12 h, then suction filter, wash with deionized water until the filtrate pH ~ 7, and dry the filter cake in a vacuum oven at 50 ° C for 12 h, The product is marked as DTM for future use.

(2)控制Co和Pt的摩尔比为Co/Pt=3将Co和Pt的前驱体盐0.75mmol CoCl2·6H2O和0.25mol H2PtCl6·6H2O,添加到20mL EG溶液中,待前驱体盐完全溶解后加入76mg DTM,搅拌一定30min后,开始从室温加热到160℃保持6h。(2) Control the molar ratio of Co and Pt to Co/Pt=3, add Co and Pt precursor salts 0.75mmol CoCl 2 ·6H 2 O and 0.25mol H 2 PtCl 6 ·6H 2 O to 20mL EG solution After the precursor salt is completely dissolved, add 76mg of DTM, stir for 30min, then start heating from room temperature to 160°C for 6h.

(3)在反应温度下降到40℃时加入76mg碳粉,搅拌4h,离心洗涤。真空条件下50℃干燥12h即可得到CoPt-3/DTM-C催化剂。(3) When the reaction temperature dropped to 40°C, 76 mg of carbon powder was added, stirred for 4 hours, and washed by centrifugation. CoPt-3/DTM-C catalyst can be obtained by drying at 50℃ for 12h under vacuum condition.

实施例3。Example 3.

(1)将硅藻土分散到40mL 3mol L-1的HCl溶液中,磁力搅拌12h,然后抽滤,用去离子水洗涤至滤液pH~7,将滤饼在真空烘箱中50℃干燥12h,产物标记为DTM备用。(1) Disperse diatomaceous earth into 40 mL of 3 mol L -1 HCl solution, stir magnetically for 12 h, then suction filter, wash with deionized water until the filtrate pH ~ 7, and dry the filter cake in a vacuum oven at 50 ° C for 12 h, The product is marked as DTM for future use.

(2)控制Co和Pt的摩尔比为Co/Pt=9将Co和Pt的前驱体盐2.25mmol CoCl2·6H2O和0.25mol H2PtCl6·6H2O,添加到20mL EG溶液中,待前驱体盐完全溶解后加入76mg DTM,搅拌一定30min后,开始从室温加热到160℃保持6h。(2) Control the molar ratio of Co and Pt to Co/Pt=9, add the precursor salt of Co and Pt 2.25mmol CoCl 2 ·6H 2 O and 0.25mol H 2 PtCl 6 ·6H 2 O to 20mL EG solution After the precursor salt is completely dissolved, add 76mg of DTM, stir for 30min, then start heating from room temperature to 160°C for 6h.

(3)在反应温度下降到40℃时加入76mg碳粉,搅拌4h,离心洗涤。真空条件下50℃干燥12h即可得到CoPt-9/DTM-C催化剂。(3) When the reaction temperature dropped to 40°C, 76 mg of carbon powder was added, stirred for 4 hours, and washed by centrifugation. CoPt-9/DTM-C catalyst can be obtained by drying at 50℃ for 12h under vacuum condition.

实例2,3的电化学测试方法与实例1相同。测试结果如图所示。实施例1中所制备的催化剂,具有最佳的氧还原催化剂性能,其起始电位为1.1V,半波电位为0.88V,极限电流密度高达5.5mA cm-2,电子转移数n为3.8~3.9,H2O2产率为2.2%~10%;Pt/C的起始电位为0.98V,半波电位为0.75V,极限电流密度为5.8mA cm-2,电子转移数n为3.88~3.94,H2O2产率为4.8%~5.5%。其起始电位、半波电位高于商业Pt/C,极限电力密度、电子转移数和H2O2产率也与商业Pt/C媲美,稳定性也非常好。CoPt-9/DTM-C具有最优的析氧性能,其在10mAcm-2电流密度下的过电位为380mV,与CoPt-9/C相比较,可以说明硅藻土的加入极大地促进了材料的析氧催化剂性能。The electrochemical testing method of example 2,3 is identical with example 1. The test results are shown in the figure. The catalyst prepared in Example 1 has the best performance as an oxygen reduction catalyst, with an initial potential of 1.1 V, a half-wave potential of 0.88 V, a limiting current density of 5.5 mA cm -2 , and an electron transfer number n of 3.8 to 3.9, the yield of H 2 O 2 is 2.2%~10%; the onset potential of Pt/C is 0.98V, the half-wave potential is 0.75V, the limiting current density is 5.8mA cm -2 , and the electron transfer number n is 3.88~ 3.94, and the yield of H 2 O 2 was 4.8%-5.5%. Its onset potential and half-wave potential are higher than those of commercial Pt/C, and its limit power density, electron transfer number and H 2 O 2 yield are also comparable to those of commercial Pt/C, and its stability is also very good. CoPt-9/DTM-C has the best oxygen evolution performance, and its overpotential at 10mAcm -2 current density is 380mV. Compared with CoPt-9/C, it can be explained that the addition of diatomite greatly promotes the Oxygen evolution catalyst performance.

上述实施例为本发明较佳的具体实施方式,但本发明的保护范围并不局限于此,其他的任何未背离本发明的精神实质与原理下所作的改变、修饰、替代、组合、简化,均应为等效的置换方式,都包含在本发明的保护范围之内。The above-mentioned embodiment is a preferred specific implementation of the present invention, but the scope of protection of the present invention is not limited thereto, and any other changes, modifications, substitutions, combinations, and simplifications that do not deviate from the spirit and principles of the present invention, All should be equivalent replacement methods, and all are included in the protection scope of the present invention.

Claims (5)

1. the preparation of bifunctional catalyst diatomite confinement cobalt platinum based composites and its electrocatalytic oxidation reduction and oxygen evolution reaction In application, it is characterised in that:Comprise the following steps:
(1) diatomite is distributed in HCl solution, is sufficiently stirred certain time, then filters, be washed with deionized to filtrate PH~7, filter cake is dried in vacuum drying oven, Product Labeling is that DTM is standby.
(2) Co and Pt mol ratio is controlled, Co and Pt precursor salt is added in EG solution, treats that precursor salt is completely dissolved After add DTM, after stirring certain time, begin to warm up.
(3) carbon dust, stirring a period of time, centrifuge washing, vacuum drying are added after dropping at the reaction temperatures.
(4) prepared catalyst series are applied in electrocatalytic oxidation reduction and oxygen evolution reaction.
2. the preparation of the bifunctional catalyst diatomite confinement cobalt platinum based composites described in claim 1 and its in electrocatalytic oxidation Application in reduction and oxygen evolution reaction, it is characterised in that:HCl concentration used in step (1) is 3mol L-1, volume 40mL, It is to remove the impurity in diatomite with the HCl purposes handled.
3. the preparation of the bifunctional catalyst diatomite confinement cobalt platinum based composites described in claim 1 and its in electrocatalytic oxidation Application in reduction and oxygen evolution reaction, it is characterised in that:Co and Pt mol ratio is Co/Pt=1, Co/Pt=3 in step (2) And Co/Pt=9, the precursor salt in step (2) is H2PtCl6·6H2O and CoCl2·6H2O, the EG volumes added are 20mL, DTM quality are 76mg, and the heating-up temperature described in step (2) is 160 DEG C, mixing time 6h.
4. the preparation of the bifunctional catalyst diatomite confinement cobalt platinum based composites described in claim 1 and its in electrocatalytic oxidation Application in reduction and oxygen evolution reaction, it is characterised in that:Step (3) temperature drops to 40 DEG C, and the quality of added carbon dust is 76mg, Mixing time is 4h.
5. the preparation of the bifunctional catalyst diatomite confinement cobalt platinum based composites described in claim 1 and its in electrocatalytic oxidation Application in reduction and oxygen evolution reaction, it is characterised in that:Step (4) test condition is:Prepared catalyst coated is taken in glass On carbon working electrode, its carrying capacity is 80.8 μ g cm-2, hydrogen reduction test environment is the 0.1mol L of oxygen saturation-1KOH electrolyte Tested under middle rotating condition, oxygen evolution reaction is in N2The 1mol L of saturation-1In KOH solution.All tests are all carried out at room temperature.
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Application publication date: 20171110