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CN103165914B - Pt/Au/PdCo/C catalyst, and preparation and application thereof - Google Patents

Pt/Au/PdCo/C catalyst, and preparation and application thereof Download PDF

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CN103165914B
CN103165914B CN201110421469.9A CN201110421469A CN103165914B CN 103165914 B CN103165914 B CN 103165914B CN 201110421469 A CN201110421469 A CN 201110421469A CN 103165914 B CN103165914 B CN 103165914B
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孙公权
唐琪雯
姜鲁华
姜黔
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Dalian Institute of Chemical Physics of CAS
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Abstract

一种Pt/Au/PdCo/C催化剂。该催化剂制备包括(1)合金化PdCo/C的制备和(2)Pt/Au/PdCo/C催化剂的制备两个步骤。该催化剂具有Pt载量低及电化学稳定性高等优点,可用作金属空气燃料电池、质子交换膜燃料电池以及直接液体燃料电池阴极氧还原催化剂。A Pt/Au/PdCo/C catalyst. The catalyst preparation includes (1) preparation of alloyed PdCo/C and (2) preparation of Pt/Au/PdCo/C catalyst. The catalyst has the advantages of low Pt loading and high electrochemical stability, and can be used as a cathode oxygen reduction catalyst for metal-air fuel cells, proton exchange membrane fuel cells, and direct liquid fuel cells.

Description

一种Pt/Au/PdCo/C催化剂及其制备和应用A kind of Pt/Au/PdCo/C catalyst and its preparation and application

技术领域 technical field

本发明涉及一种氧还原催化剂,具体的说涉及一种用于金属空气燃料电池氧还原催化剂、质子交换膜燃料电池氧还原催化剂、直接液体燃料电池氧还原催化剂的制备和应用。The invention relates to an oxygen reduction catalyst, in particular to the preparation and application of an oxygen reduction catalyst for a metal-air fuel cell, an oxygen reduction catalyst for a proton exchange membrane fuel cell, and an oxygen reduction catalyst for a direct liquid fuel cell.

背景技术 Background technique

随着煤炭、石油和天然气等燃料的消耗量与日剧增及能源资源的储量日益枯竭,寻找环境友好可持续发展的能源技术迫在眉睫。燃料电池因其具有能量转化效率高、无污染、无噪音等优点,已成为世界各国研究的热点。With the increasing consumption of fuels such as coal, oil and natural gas and the depletion of energy resources, it is urgent to find energy technologies that are environmentally friendly and sustainable. Because of its high energy conversion efficiency, no pollution, no noise and other advantages, fuel cells have become a research hotspot all over the world.

目前,燃料电池阴极ORR催化剂最有效的催化剂仍然是Pt及其合金催化剂。而Pt有限的储量和高昂的价格成为燃料电池商业化的障碍之一。如何在不降低催化剂活性的前提下提高其利用率成为近来的研究热点。At present, the most effective catalysts for fuel cell cathode ORR catalysts are still Pt and its alloy catalysts. However, the limited reserves and high price of Pt have become one of the obstacles to the commercialization of fuel cells. How to increase the utilization of catalysts without reducing their activity has become a research hotspot recently.

Adzic研究组发现通过Cu-UPD在贵金属粒子表面形成单层Cu原子,再与Pt2+进行置换得到Pt单层催化剂,其中内核一般采用Pd、Au等贵金属及其合金。高度分散的Pt使得该类催化剂的ORR比质量活性大大提高。然而,对于该类催化剂在电化学环境下稳定性的研究较少。Adzic's research group found that a single layer of Cu atoms was formed on the surface of noble metal particles through Cu-UPD, and then replaced with Pt 2+ to obtain a Pt single layer catalyst, in which noble metals such as Pd, Au and their alloys were generally used as the inner core. The highly dispersed Pt greatly improves the ORR specific mass activity of this type of catalyst. However, there are few studies on the stability of such catalysts in electrochemical environments.

对Pt/PdCo/C催化剂进行加速老化试验,在0.6-1.0V vs.NHE的电势范围内以100mV s-1的扫速进行CV扫描,10k圈之后ORR极化曲线的半波电位负移34mV,催化活性明显衰减,说明在催化剂表面高度分散的Pt单层电化学稳定性较差。Au纳米粒子具有良好的电化学稳定性,将其引入到电催化剂中可以大大地改善电催化剂的稳定性。然而,Au本身的ORR催化活性较差,若将其引入催化剂中时覆盖了Pt的活性位可能导致催化活性的降低。为此,我们设计通过Cu-UPD-置换的方法将Au作为次单层引入到表面Pt层和PdCo核之间,旨在不降低ORR催化活性的前提下提高Pt单层催化剂的电化学稳定性。The accelerated aging test was carried out on Pt/PdCo/C catalyst, and the CV scan was performed at a scan rate of 100mV s -1 in the potential range of 0.6-1.0V vs. NHE, and the half-wave potential of the ORR polarization curve shifted negatively by 34mV after 10k cycles , the catalytic activity was obviously attenuated, indicating that the highly dispersed Pt monolayer on the surface of the catalyst had poor electrochemical stability. Au nanoparticles have good electrochemical stability, and their introduction into electrocatalysts can greatly improve the stability of electrocatalysts. However, the ORR catalytic activity of Au itself is poor, and if it is introduced into the catalyst to cover the active sites of Pt, the catalytic activity may decrease. To this end, we designed a Cu-UPD-replacement method to introduce Au as a sub-monolayer between the surface Pt layer and the PdCo core, aiming at improving the electrochemical stability of the Pt monolayer catalyst without reducing the catalytic activity of ORR. .

发明内容 Contents of the invention

针对现有技术的不足,本发明目的在于提供一种用于金属空气燃料电池氧还原催化剂、质子交换膜燃料电池氧还原催化剂、直接液体燃料电池氧还原催化剂的制备和应用。Aiming at the deficiencies of the prior art, the purpose of the present invention is to provide a preparation and application of an oxygen reduction catalyst for a metal-air fuel cell, an oxygen reduction catalyst for a proton exchange membrane fuel cell, and an oxygen reduction catalyst for a direct liquid fuel cell.

为实现上述目的,本发明采用以下具体方案来实现:In order to achieve the above object, the present invention adopts the following specific solutions to achieve:

一种Pt/Au/PdCo/C催化剂,Pt在纳米粒子表面分布,Au位于Pt壳与PdCo核之间。催化剂中金属质量占总质量的12-46%;其中Pd和Co的摩尔比为5∶1-1∶1;Pd和Au的摩尔比为5∶1-12∶1;Pd和Pt的摩尔比为10∶1-20∶1。A Pt/Au/PdCo/C catalyst, Pt is distributed on the surface of nanoparticles, and Au is located between the Pt shell and the PdCo core. The metal mass in the catalyst accounts for 12-46% of the total mass; wherein the molar ratio of Pd and Co is 5:1-1:1; the molar ratio of Pd and Au is 5:1-12:1; the molar ratio of Pd and Pt It is 10:1-20:1.

所述催化剂的制备方法,包括以下步骤,The preparation method of described catalyst comprises the following steps,

(1)合金化PdCo/C的制备(1) Preparation of Alloyed PdCo/C

a.于去离子水中加入PdCl2和/或Pd(NO3)2,同时加入Co(NO3)2、CoCl2、CoBr2、CoSO4、Co(COOH)2中的一种或两种以上,形成混合物,搅拌使之混合均匀,之后于混合液中加入碳载体,并超声分散至混合液均匀;a. Add PdCl 2 and/or Pd(NO 3 ) 2 to deionized water, and at the same time add one or more of Co(NO 3 ) 2 , CoCl 2 , CoBr 2 , CoSO 4 , Co(COOH) 2 , form a mixture, stir to make it evenly mixed, then add carbon carrier to the mixed liquid, and ultrasonically disperse until the mixed liquid is uniform;

b.于上述步骤(1)a所得混合液中滴加柠檬酸钠水溶液,并在快速搅拌的条件下逐滴滴加NaBH4水溶液,静置后过滤得固体物质,之后采用去离子水对所得固体物质进行洗涤,并将洗涤后所得物质置于真空烘箱中干燥,得PdCo/C;b. Add sodium citrate aqueous solution dropwise in the mixed solution obtained in the above step (1) a, and add dropwise NaBH aqueous solution under the condition of rapid stirring, filter to obtain solid matter after standing, and then use deionized water to obtain The solid matter is washed, and the obtained matter after washing is placed in a vacuum oven to dry to obtain PdCo/C;

c.将步骤(1)b所得PdCo/C于氢气和惰性气体混合气中进行热处理,得合金化PdCo/C;c. heat-treating the PdCo/C obtained in step (1)b in a mixture of hydrogen and an inert gas to obtain alloyed PdCo/C;

(2)Pt/Au/PdCo/C催化剂的制备(2) Preparation of Pt/Au/PdCo/C catalyst

a.于乙醇中,加入上述步骤(1)c所得合金化PdCo/C,搅拌使之混合均匀后加入Nafion乳液,并超声分散至混合液均匀;a. In ethanol, add the alloyed PdCo/C obtained in the above step (1) c, stir to make it evenly mixed, then add Nafion emulsion, and ultrasonically disperse until the mixture is uniform;

b.移取上述步骤(2)a所得混合液,并涂覆于玻碳电极表面作为工作电极,对电极和参比电极分别为Pt丝和饱和甘汞电极;b. pipette the mixed solution obtained in the above step (2) a, and apply it to the surface of the glassy carbon electrode as a working electrode, and the counter electrode and the reference electrode are respectively Pt wire and a saturated calomel electrode;

c.将上述步骤(2)b所得工作电极置于H2SO4和CuSO4混合溶液中并在350-520mV的沉积电位下维持1-300s,然后快速将电极浸入H2SO4和HAuCl4混合溶液中并静置1-10min进行置换反应,再用去离子水将电极清洗干净;c. Place the working electrode obtained in the above step (2)b in the mixed solution of H 2 SO 4 and CuSO 4 and maintain it at a deposition potential of 350-520mV for 1-300s, then quickly immerse the electrode in H 2 SO 4 and HAuCl 4 Put it in the mixed solution and let it stand for 1-10min to carry out the replacement reaction, and then clean the electrode with deionized water;

d.将上述步骤(2)c所得工作电极置于H2SO4和CuSO4混合溶液中在350-520mV的沉积电位下维持1-300s,然后快速将电极浸入H2SO4和K2PtCl4混合溶液中并静置1-10min进行置换反应,再用去离子水将电极清洗干净,即得到Pt/Au/PdCo/C催化剂。d. Place the working electrode obtained in the above step (2)c in the mixed solution of H 2 SO 4 and CuSO 4 at a deposition potential of 350-520mV for 1-300s, then quickly immerse the electrode in H 2 SO 4 and K 2 PtCl 4 Put it in the mixed solution and let it stand for 1-10min to carry out the replacement reaction, and then clean the electrode with deionized water to obtain the Pt/Au/PdCo/C catalyst.

步骤(1)a中所述混合物中Pd2+和Co2+的摩尔比为5∶1-1∶1;所述混合物中Pd2+的浓度为10-100mmol L-1The molar ratio of Pd 2+ and Co 2+ in the mixture in step (1)a is 5:1-1:1; the concentration of Pd 2+ in the mixture is 10-100mmol L -1 .

步骤(1)中所述合金化PdCo/C中的金属质量占总质量的10-40%。The metal mass in the alloyed PdCo/C in step (1) accounts for 10-40% of the total mass.

步骤(1)b中所述柠檬酸钠水溶液的浓度为10-50mmol L-1,用量为10-50mL;所述NaBH4水溶液的浓度为10-100mmol L-1,用量为10-50mL;所述真空干燥时间为5-20小时。The concentration of the sodium citrate aqueous solution in step (1)b is 10-50mmol L -1 , and the dosage is 10-50mL; the concentration of the NaBH 4 aqueous solution is 10-100mmol L -1 , and the dosage is 10-50mL; The vacuum drying time is 5-20 hours.

步骤(1)c中所述惰性气氛为氩气、氦气、氮气中的一种或一种以上的混合物;所述氢气体积占气体总体积的1-10%;所述热处理温度为200-600℃,所述热处理时间为1-3小时;The inert atmosphere described in the step (1) c is a mixture of one or more of argon, helium, nitrogen; the hydrogen volume accounts for 1-10% of the total gas volume; the heat treatment temperature is 200- 600°C, the heat treatment time is 1-3 hours;

步骤(2)a中所述PdCo/C于乙醇中的浓度为0.5-5mg mL-1;所述Nafion与PdCo/C的质量比为1∶10-1∶1。The concentration of PdCo/C in ethanol in step (2)a is 0.5-5 mg mL -1 ; the mass ratio of Nafion to PdCo/C is 1:10-1:1.

步骤(2)c和步骤(2)d中所述H2SO4和CuSO4混合溶液中二者的物质量比为5∶1-1∶2;所述H2SO4和HAuCl4混合溶液中二者的物质量比为100∶1-20∶1;所述H2SO4和K2PtCl4混合溶液中二者的物质量比为100∶1-20∶1;所述H2SO4的物质量浓度为20-100mmol L-1The mass ratio of H2SO4 and CuSO4 in the mixed solution of step (2 ) c and step (2)d is 5:1-1: 2 ; the mixed solution of H2SO4 and HAuCl4 The mass ratio of the two in the H2SO4 and K2PtCl4 mixed solution is 100:1-20:1; the mass ratio of the two in the H2SO4 and K2PtCl4 mixed solution is 100:1-20:1; the H2SO The substance concentration of 4 is 20-100mmol L -1 .

所述碳载体为:XC-72R、BP2000、乙炔黑、碳纳米管、石墨中的一种或两种以上的混合物;The carbon carrier is: one or a mixture of two or more of XC-72R, BP2000, acetylene black, carbon nanotubes, and graphite;

所述Pt/Au/PdCo/C催化剂可用作金属空气燃料电池氧还原催化剂、质子交换膜燃料电池氧还原催化剂、直接液体燃料电池氧还原催化剂。The Pt/Au/PdCo/C catalyst can be used as an oxygen reduction catalyst for a metal-air fuel cell, an oxygen reduction catalyst for a proton exchange membrane fuel cell, or an oxygen reduction catalyst for a direct liquid fuel cell.

与现有技术相比,本发明所述新型Pt/Au/PdCo/C催化剂具有以下优点:Compared with the prior art, the novel Pt/Au/PdCo/C catalyst of the present invention has the following advantages:

1.贵金属Pt在纳米粒子表面分布,降低了Pt的载量,从而降低了催化剂的成本1. The noble metal Pt is distributed on the surface of the nanoparticles, which reduces the loading of Pt, thereby reducing the cost of the catalyst

2.将具有良好电化学稳定性的Au引入到Pt壳和PdCo核之间,大大提高了Pt单层催化剂的ORR活性和电化学稳定性。2. The introduction of Au with good electrochemical stability between the Pt shell and the PdCo core greatly improves the ORR activity and electrochemical stability of the Pt monolayer catalyst.

附图说明 Description of drawings

图1为在不同欠电位下沉积的Cu的溶出曲线(根据实施例1-5);Fig. 1 is the stripping curve (according to embodiment 1-5) of Cu deposited under different underpotentials;

图2为经过不同时间欠电位沉积的Cu的溶出曲线(根据实施例3和6-8);Fig. 2 is the stripping curve (according to embodiment 3 and 6-8) of the Cu of underpotential deposition through different time;

图3为根据实施例1和比较例3制备得到的样品在0.1M HClO4溶液中的循环伏安(CV)曲线和氧还原反应(ORR)极化曲线;Fig. 3 is the cyclic voltammetry (CV) curve and the oxygen reduction reaction (ORR) polarization curve of the sample prepared according to embodiment 1 and comparative example 3 in 0.1M HClO solution;

图4为根据实施例1和比较例3制备得到的样品在0.1M HClO4溶液中稳定性测试前后的CV曲线和ORR极化曲线;Fig. 4 is the CV curve and the ORR polarization curve of the sample prepared according to embodiment 1 and comparative example 3 before and after the stability test in 0.1M HClO solution;

图5为根据实施例1和比较例3制备得到的样品在0.1M HClO4溶液中稳定性测试前后的TEM照片;Fig. 5 is the TEM photo before and after the stability test of the sample prepared according to embodiment 1 and comparative example 3 in 0.1M HClO solution;

图6为根据实施例1和比较例2制备得到的样品在0.1M HClO4溶液中稳定性测试前后的TEM照片。FIG. 6 is a TEM photo of the samples prepared according to Example 1 and Comparative Example 2 before and after the stability test in 0.1M HClO 4 solution.

具体实施方式: Detailed ways:

下面结合实施例对本发明作详细的描述。当然本发明并不仅限于这些具体的实施例。Below in conjunction with embodiment the present invention is described in detail. Of course, the present invention is not limited to these specific examples.

实施例1:Example 1:

称取28.2mg PdCl2和9.6mg Co(NO3)2(Pd/Co原子比为3∶1)溶于100mL去离子水中,加入80mg Vulcan XC-72碳粉并超声分散30min。待分散均匀后滴加25mmol L-1柠檬酸钠水溶液25mL,然后在快速搅拌下缓慢滴加80mmol L-1 NaBH4溶液25mL。30min后将得到的产物过滤,大量去离子水洗涤,80℃真空烘箱干燥8h,得到PdCo/C催化剂。将PdCo/C催化剂于400℃、5vol%H2/Ar气氛下热处理2h即可得到合金化的PdCo/C催化剂。Weigh 28.2mg PdCl 2 and 9.6mg Co(NO 3 ) 2 (Pd/Co atomic ratio is 3:1) and dissolve in 100mL deionized water, add 80mg Vulcan XC-72 carbon powder and ultrasonically disperse for 30min. After uniform dispersion, 25mL of 25mmol L -1 sodium citrate aqueous solution was added dropwise, and then 25mL of 80mmol L -1 NaBH 4 solution was slowly added dropwise under rapid stirring. After 30 minutes, the obtained product was filtered, washed with a large amount of deionized water, and dried in a vacuum oven at 80° C. for 8 hours to obtain a PdCo/C catalyst. The alloyed PdCo/C catalyst can be obtained by heat-treating the PdCo/C catalyst at 400° C. for 2 hours under a 5vol% H 2 /Ar atmosphere.

将5mg合金化的PdCo/C催化剂分散于2mL乙醇中,加入30μL 5%Nafion乳液作粘结剂。超声分散15min后移取20μL浆液涂覆于玻碳电极表面作为工作电极。将工作电极置于50mmol L-1 H2SO4和50mmol L-1CuSO4混合溶液中进行Cu欠电位沉积:首先在350mV的沉积电位维持120s使Cu在PdCo纳米粒子表面发生欠电位沉积,然后快速将电极浸入50mmolL-1 H2SO4和1mmol L-1 HAuCl4混合溶液中,静置4min使Au3+与Cu2+发生置换反应,然后用去离子水将电极表面清洗干净。重复进行Cu的欠电位沉积,然后将电极快速置于50mmol L-1 H2SO4和1mmol L-1 K2PtCl4混合溶液中,静置4min使Pt2+与Cu2+发生置换反应,然后用去离子水将电极清洗干净即可得到Pt/Au/PdCo/C催化剂。Disperse 5 mg of alloyed PdCo/C catalyst in 2 mL of ethanol, and add 30 μL of 5% Nafion emulsion as a binder. After ultrasonic dispersion for 15 min, 20 μL of the slurry was pipetted and coated on the surface of a glassy carbon electrode as a working electrode. The working electrode was placed in a mixed solution of 50mmol L -1 H 2 SO 4 and 50mmol L -1 CuSO 4 for Cu underpotential deposition: first, the deposition potential of 350mV was maintained for 120s to make Cu underpotential deposition on the surface of PdCo nanoparticles, and then Quickly immerse the electrode in the mixed solution of 50mmolL -1 H 2 SO 4 and 1mmol L -1 HAuCl 4 , let it stand for 4min to make the replacement reaction between Au 3+ and Cu 2+ , and then clean the surface of the electrode with deionized water. The underpotential deposition of Cu was repeated, and then the electrode was quickly placed in the mixed solution of 50mmol L -1 H 2 SO 4 and 1mmol L -1 K 2 PtCl 4 , and stood for 4min to allow the substitution reaction between Pt 2+ and Cu 2+ , Then the electrode is cleaned with deionized water to obtain the Pt/Au/PdCo/C catalyst.

实施例2:Example 2:

称取28.2mg PdCl2和9.6mg Co(NO3)2(Pd/Co原子比为3∶1)溶于100mL去离子水中,加入80mg Vulcan XC-72碳粉并超声分散30min。待分散均匀后滴加25mmol L-1柠檬酸钠水溶液25mL,然后在快速搅拌下缓慢滴加80mmol L-1 NaBH4溶液25mL。30min后将得到的产物过滤,大量去离子水洗涤,80℃真空烘箱干燥8h,得到PdCo/C催化剂。将PdCo/C催化剂于400℃、5vol%H2/Ar气氛下热处理2h即可得到合金化的PdCo/C催化剂。Weigh 28.2mg PdCl 2 and 9.6mg Co(NO 3 ) 2 (Pd/Co atomic ratio is 3:1) and dissolve in 100mL deionized water, add 80mg Vulcan XC-72 carbon powder and ultrasonically disperse for 30min. After uniform dispersion, 25mL of 25mmol L -1 sodium citrate aqueous solution was added dropwise, and then 25mL of 80mmol L -1 NaBH 4 solution was slowly added dropwise under rapid stirring. After 30 minutes, the obtained product was filtered, washed with a large amount of deionized water, and dried in a vacuum oven at 80° C. for 8 hours to obtain a PdCo/C catalyst. The alloyed PdCo/C catalyst can be obtained by heat-treating the PdCo/C catalyst at 400° C. for 2 hours under a 5vol% H 2 /Ar atmosphere.

将5mg合金化的PdCo/C催化剂分散于2mL乙醇中,加入30μL 5%Nafion乳液作粘结剂。超声分散15min后移取20μL浆液涂覆于玻碳电极表面作为工作电极。将工作电极置于50mmol L-1 H2SO4和50mmol L-1CuSO4混合溶液中进行Cu欠电位沉积:首先在370mV的沉积电位维持120s使Cu在PdCo纳米粒子表面发生欠电位沉积,然后快速将电极浸入50mmolL-1 H2SO4和1mmol L-1 HAuCl4混合溶液中,静置4min使Au3+与Cu2+发生置换反应,然后用去离子水将电极表面清洗干净。重复进行Cu的欠电位沉积,然后将电极快速置于50mmol L-1 H2SO4和1mmol L-1 K2PtCl4混合溶液中,静置4min使Pt2+与Cu2+发生置换反应,然后用去离子水将电极清洗干净即可得到Pt/Au/PdCo/C催化剂。Disperse 5 mg of alloyed PdCo/C catalyst in 2 mL of ethanol, and add 30 μL of 5% Nafion emulsion as a binder. After ultrasonic dispersion for 15 min, 20 μL of the slurry was pipetted and coated on the surface of a glassy carbon electrode as a working electrode. The working electrode was placed in a mixed solution of 50mmol L -1 H 2 SO 4 and 50mmol L -1 CuSO 4 for Cu underpotential deposition: first, the deposition potential of 370mV was maintained for 120s to make Cu underpotential deposition on the surface of PdCo nanoparticles, and then Quickly immerse the electrode in the mixed solution of 50mmolL -1 H 2 SO 4 and 1mmol L -1 HAuCl 4 , let it stand for 4min to make the replacement reaction between Au 3+ and Cu 2+ , and then clean the surface of the electrode with deionized water. The underpotential deposition of Cu was repeated, and then the electrode was quickly placed in the mixed solution of 50mmol L -1 H 2 SO 4 and 1mmol L -1 K 2 PtCl 4 , and stood for 4min to allow the substitution reaction between Pt 2+ and Cu 2+ , Then the electrode is cleaned with deionized water to obtain the Pt/Au/PdCo/C catalyst.

实施例3:Example 3:

称取28.2mg PdCl2和9.6mg Co(NO3)2(Pd/Co原子比为3∶1)溶于100mL去离子水中,加入80mg Vulcan XC-72碳粉并超声分散30min。待分散均匀后滴加25mmol L-1柠檬酸钠水溶液25mL,然后在快速搅拌下缓慢滴加80mmol L-1 NaBH4溶液25mL。30min后将得到的产物过滤,大量去离子水洗涤,80℃真空烘箱干燥8h,得到PdCo/C催化剂。将PdCo/C催化剂于400℃、5vol%H2/Ar气氛下热处理2h即可得到合金化的PdCo/C催化剂。Weigh 28.2mg PdCl 2 and 9.6mg Co(NO 3 ) 2 (Pd/Co atomic ratio is 3:1) and dissolve in 100mL deionized water, add 80mg Vulcan XC-72 carbon powder and ultrasonically disperse for 30min. After uniform dispersion, 25mL of 25mmol L -1 sodium citrate aqueous solution was added dropwise, and then 25mL of 80mmol L -1 NaBH 4 solution was slowly added dropwise under rapid stirring. After 30 minutes, the obtained product was filtered, washed with a large amount of deionized water, and dried in a vacuum oven at 80° C. for 8 hours to obtain a PdCo/C catalyst. The alloyed PdCo/C catalyst can be obtained by heat-treating the PdCo/C catalyst at 400° C. for 2 hours under a 5vol% H 2 /Ar atmosphere.

将5mg合金化的PdCo/C催化剂分散于2mL乙醇中,加入30μL 5%Nafion乳液作粘结剂。超声分散15min后移取20μL浆液涂覆于玻碳电极表面作为工作电极。将工作电极置于50mmol L-1 H2SO4和50mmol L-1CuSO4混合溶液中进行Cu欠电位沉积:首先在390mV的沉积电位维持120s使Cu在PdCo纳米粒子表面发生欠电位沉积,然后快速将电极浸入50mmolL-1 H2SO4和1mmol L-1 HAuCl4混合溶液中,静置4min使Au3+与Cu2+发生置换反应,然后去离子水将电极表面清洗干净。重复进行Cu的欠电位沉积,然后将电极快速置于50mmol L-1 H2SO4和1mmol L-1 K2PtCl4混合溶液中,静置4min使Pt2+与Cu2+发生置换反应,然后去离子水将电极清洗干净即可得到Pt/Au/PdCo/C催化剂。Disperse 5 mg of alloyed PdCo/C catalyst in 2 mL of ethanol, and add 30 μL of 5% Nafion emulsion as a binder. After ultrasonic dispersion for 15 min, 20 μL of the slurry was pipetted and coated on the surface of a glassy carbon electrode as a working electrode. The working electrode was placed in a mixed solution of 50mmol L -1 H 2 SO 4 and 50mmol L -1 CuSO 4 for Cu underpotential deposition: first, the deposition potential of 390mV was maintained for 120s to make Cu underpotential deposition on the surface of PdCo nanoparticles, and then Quickly immerse the electrode in the mixed solution of 50mmolL -1 H 2 SO 4 and 1mmol L -1 HAuCl 4 , let it stand for 4min to make the replacement reaction between Au 3+ and Cu 2+ , and then clean the surface of the electrode with deionized water. The underpotential deposition of Cu was repeated, and then the electrode was quickly placed in the mixed solution of 50mmol L -1 H 2 SO 4 and 1mmol L -1 K 2 PtCl 4 , and stood for 4min to allow the substitution reaction between Pt 2+ and Cu 2+ , Then the electrode is cleaned with deionized water to obtain the Pt/Au/PdCo/C catalyst.

实施例4:Example 4:

称取28.2mg PdCl2和9.6mg Co(NO3)2(Pd/Co原子比为3∶1)溶于100mL去离子水中,加入80mg Vulcan XC-72碳粉并超声分散30min。待分散均匀后滴加25mmol L-1柠檬酸钠水溶液25mL,然后在快速搅拌下缓慢滴加80mmol L-1 NaBH4溶液25mL。30min后将得到的产物过滤,大量去离子水洗涤,80℃真空烘箱干燥8h,得到PdCo/C催化剂。将PdCo/C催化剂于400℃、5vol%H2/Ar气氛下热处理2h即可得到合金化的PdCo/C催化剂。Weigh 28.2mg PdCl 2 and 9.6mg Co(NO 3 ) 2 (Pd/Co atomic ratio is 3:1) and dissolve in 100mL deionized water, add 80mg Vulcan XC-72 carbon powder and ultrasonically disperse for 30min. After uniform dispersion, 25mL of 25mmol L -1 sodium citrate aqueous solution was added dropwise, and then 25mL of 80mmol L -1 NaBH 4 solution was slowly added dropwise under rapid stirring. After 30 minutes, the obtained product was filtered, washed with a large amount of deionized water, and dried in a vacuum oven at 80° C. for 8 hours to obtain a PdCo/C catalyst. The alloyed PdCo/C catalyst can be obtained by heat-treating the PdCo/C catalyst at 400° C. for 2 hours under a 5vol% H 2 /Ar atmosphere.

将5mg合金化的PdCo/C催化剂分散于2mL乙醇中,加入30μL 5%Nafion乳液作粘结剂。超声分散15min后移取20μL浆液涂覆于玻碳电极表面作为工作电极。将工作电极置于50mmol L-1 H2SO4和50mmol L-1CuSO4溶液中进行Cu欠电位沉积:首先在420mV的沉积电位维持120s使Cu在PdCo纳米粒子表面发生欠电位沉积,然后快速将电极浸入50mmol L-1H2SO4和1mmol L-1 HAuCl4混合溶液中,静置4min使Au3+与Cu2+发生置换反应,然后用去离子水将电极表面清洗干净。重复进行Cu的欠电位沉积,然后将电极快速置于50mmol L-1 H2SO4和1mmol L-1 K2PtCl4溶液中,静置4min使Pt2+与Cu2+发生置换反应,然后用去离子水将电极清洗干净即可得到Pt/Au/PdCo/C催化剂。Disperse 5 mg of alloyed PdCo/C catalyst in 2 mL of ethanol, and add 30 μL of 5% Nafion emulsion as a binder. After ultrasonic dispersion for 15 min, 20 μL of the slurry was pipetted and coated on the surface of a glassy carbon electrode as a working electrode. Place the working electrode in a solution of 50mmol L -1 H 2 SO 4 and 50mmol L -1 CuSO 4 for Cu underpotential deposition: first, maintain a deposition potential of 420mV for 120s to cause underpotential deposition of Cu on the surface of PdCo nanoparticles, and then quickly Immerse the electrode in a mixed solution of 50mmol L -1 H 2 SO 4 and 1mmol L -1 HAuCl 4 , let it stand for 4min to make the replacement reaction between Au 3+ and Cu 2+ , and then clean the surface of the electrode with deionized water. Repeat the underpotential deposition of Cu, then quickly place the electrode in the solution of 50mmol L -1 H 2 SO 4 and 1mmol L -1 K 2 PtCl 4 , let it stand for 4min to allow the substitution reaction between Pt 2+ and Cu 2+ , then Clean the electrode with deionized water to obtain the Pt/Au/PdCo/C catalyst.

实施例5:Example 5:

称取28.2mg PdCl2和9.6mg Co(NO3)2(Pd/Co原子比为3∶1)溶于100mL去离子水中,加入80mg Vulcan XC-72碳粉并超声分散30min。待分散均匀后滴加25mmol L-1柠檬酸钠水溶液25mL,然后在快速搅拌下缓慢滴加80mmol L-1 NaBH4溶液25mL。30min后将得到的产物过滤,大量去离子水洗涤,80℃真空烘箱干燥8h,得到PdCo/C催化剂。将PdCo/C催化剂于400℃、5vol%H2/Ar气氛下热处理2h即可得到合金化的PdCo/C催化剂。Weigh 28.2mg PdCl 2 and 9.6mg Co(NO 3 ) 2 (Pd/Co atomic ratio is 3:1) and dissolve in 100mL deionized water, add 80mg Vulcan XC-72 carbon powder and ultrasonically disperse for 30min. After uniform dispersion, 25mL of 25mmol L -1 sodium citrate aqueous solution was added dropwise, and then 25mL of 80mmol L -1 NaBH 4 solution was slowly added dropwise under rapid stirring. After 30 minutes, the obtained product was filtered, washed with a large amount of deionized water, and dried in a vacuum oven at 80° C. for 8 hours to obtain a PdCo/C catalyst. The alloyed PdCo/C catalyst can be obtained by heat-treating the PdCo/C catalyst at 400° C. for 2 hours under a 5vol% H 2 /Ar atmosphere.

将5mg合金化的PdCo/C催化剂分散于2mL乙醇中,加入30μL 5%Nafion乳液作粘结剂。超声分散15min后移取20μL浆液涂覆于玻碳电极表面作为工作电极。将工作电极置于50mmol L-1 H2SO4和50mmol L-1CuSO4混合溶液中进行Cu欠电位沉积:首先在520mV的沉积电位维持120s使Cu在PdCo纳米粒子表面发生欠电位沉积,然后快速将电极浸入50mmolL-1 H2SO4和1mmol L-1 HAuCl4混合溶液中,静置4min使Au3+与Cu2+发生置换反应,然后用去离子水将电极表面清洗干净。重复进行Cu的欠电位沉积,然后将电极快速置于50mmol L-1 H2SO4和1mmol L-1 K2PtCl4混合溶液中,静置4min使Pt2+与Cu2+发生置换反应,然后用去离子水将电极清洗干净即可得到Pt/Au/PdCo/C催化剂。Disperse 5 mg of alloyed PdCo/C catalyst in 2 mL of ethanol, and add 30 μL of 5% Nafion emulsion as a binder. After ultrasonic dispersion for 15 min, 20 μL of the slurry was pipetted and coated on the surface of a glassy carbon electrode as a working electrode. The working electrode was placed in a mixed solution of 50mmol L -1 H 2 SO 4 and 50mmol L -1 CuSO 4 for Cu underpotential deposition: first, the deposition potential of 520mV was maintained for 120s to make Cu underpotential deposition on the surface of PdCo nanoparticles, and then Quickly immerse the electrode in the mixed solution of 50mmolL -1 H 2 SO 4 and 1mmol L -1 HAuCl 4 , let it stand for 4min to make the replacement reaction between Au 3+ and Cu 2+ , and then clean the surface of the electrode with deionized water. The underpotential deposition of Cu was repeated, and then the electrode was quickly placed in the mixed solution of 50mmol L -1 H 2 SO 4 and 1mmol L -1 K 2 PtCl 4 , and stood for 4min to allow the substitution reaction between Pt 2+ and Cu 2+ , Then the electrode is cleaned with deionized water to obtain the Pt/Au/PdCo/C catalyst.

实施例6:Embodiment 6:

称取28.2mg PdCl2和9.6mg Co(NO3)2(Pd/Co原子比为3∶1)溶于100mL去离子水中,加入80mg Vulcan XC-72碳粉并超声分散30min。待分散均匀后滴加25mmol L-1柠檬酸钠水溶液25mL,然后在快速搅拌下缓慢滴加80mmol L-1 NaBH4溶液25mL。30min后将得到的产物过滤,大量去离子水洗涤,80℃真空烘箱干燥8h,得到PdCo/C催化剂。将PdCo/C催化剂于400℃、5vol%H2/Ar气氛下热处理2h即可得到合金化的PdCo/C催化剂。Weigh 28.2mg PdCl 2 and 9.6mg Co(NO 3 ) 2 (Pd/Co atomic ratio is 3:1) and dissolve in 100mL deionized water, add 80mg Vulcan XC-72 carbon powder and ultrasonically disperse for 30min. After uniform dispersion, 25mL of 25mmol L -1 sodium citrate aqueous solution was added dropwise, and then 25mL of 80mmol L -1 NaBH 4 solution was slowly added dropwise under rapid stirring. After 30 minutes, the obtained product was filtered, washed with a large amount of deionized water, and dried in a vacuum oven at 80° C. for 8 hours to obtain a PdCo/C catalyst. The alloyed PdCo/C catalyst can be obtained by heat-treating the PdCo/C catalyst at 400° C. for 2 hours under a 5vol% H 2 /Ar atmosphere.

将5mg合金化的PdCo/C催化剂分散于2mL乙醇中,加入30μL 5%Nafion乳液作粘结剂。超声分散15min后移取20μL浆液涂覆于玻碳电极表面作为工作电极。将工作电极置于50mmol L-1 H2SO4和50mmol L-1CuSO4混合溶液中进行Cu欠电位沉积:首先在390mV的沉积电位维持1s使Cu在PdCo纳米粒子表面发生欠电位沉积,然后快速将电极浸入50mmol L-1H2SO4和1mmol L-1 HAuCl4溶液中,静置4min使Au3+与Cu2+发生置换反应,然后去离子水将电极表面清洗干净。重复进行Cu的欠电位沉积,然后将电极快速置于50mmol L-1 H2SO4和1mmol L-1 K2PtCl4混合溶液中,静置4min使Pt2+与Cu2+发生置换反应,然后去离子水将电极清洗干净即可得到Pt/Au/PdCo/C催化剂。Disperse 5 mg of alloyed PdCo/C catalyst in 2 mL of ethanol, and add 30 μL of 5% Nafion emulsion as a binder. After ultrasonic dispersion for 15 min, 20 μL of the slurry was pipetted and coated on the surface of a glassy carbon electrode as a working electrode. The working electrode was placed in a mixed solution of 50mmol L -1 H 2 SO 4 and 50mmol L -1 CuSO 4 for Cu underpotential deposition: firstly, the deposition potential of 390mV was maintained for 1s to cause underpotential deposition of Cu on the surface of PdCo nanoparticles, and then Quickly immerse the electrode in a solution of 50mmol L -1 H 2 SO 4 and 1mmol L -1 HAuCl 4 , let it stand for 4 minutes to allow the substitution reaction between Au 3+ and Cu 2+ , and then clean the surface of the electrode with deionized water. The underpotential deposition of Cu was repeated, and then the electrode was quickly placed in the mixed solution of 50mmol L -1 H 2 SO 4 and 1mmol L -1 K 2 PtCl 4 , and stood for 4min to allow the substitution reaction between Pt 2+ and Cu 2+ , Then the electrode is cleaned with deionized water to obtain the Pt/Au/PdCo/C catalyst.

实施例7:Embodiment 7:

称取28.2mg PdCl2和9.6mg Co(NO3)2(Pd/Co原子比为3∶1)溶于100mL去离子水中,加入80mg Vulcan XC-72碳粉并超声分散30min。待分散均匀后滴加25mmol L-1柠檬酸钠水溶液25mL,然后在快速搅拌下缓慢滴加80mmol L-1 NaBH4溶液25mL。30min后将得到的产物过滤,大量去离子水洗涤,80℃真空烘箱干燥8h,得到PdCo/C催化剂。将PdCo/C催化剂于400℃、5vol%H2/Ar气氛下热处理2h即可得到合金化的PdCo/C催化剂。Weigh 28.2mg PdCl 2 and 9.6mg Co(NO 3 ) 2 (Pd/Co atomic ratio is 3:1) and dissolve in 100mL deionized water, add 80mg Vulcan XC-72 carbon powder and ultrasonically disperse for 30min. After uniform dispersion, 25mL of 25mmol L -1 sodium citrate aqueous solution was added dropwise, and then 25mL of 80mmol L -1 NaBH 4 solution was slowly added dropwise under rapid stirring. After 30 minutes, the obtained product was filtered, washed with a large amount of deionized water, and dried in a vacuum oven at 80° C. for 8 hours to obtain a PdCo/C catalyst. The alloyed PdCo/C catalyst can be obtained by heat-treating the PdCo/C catalyst at 400° C. for 2 hours under a 5vol% H 2 /Ar atmosphere.

将5mg合金化的PdCo/C催化剂分散于2mL乙醇中,加入30μL 5%Nafion乳液作粘结剂。超声分散15min后移取20μL浆液涂覆于玻碳电极表面作为工作电极。将工作电极置于50mmol L-1 H2SO4和50mmol L-1CuSO4混合溶液中进行Cu欠电位沉积:首先在390mV的沉积电位维持40s使Cu在PdCo纳米粒子表面发生欠电位沉积,然后快速将电极浸入50mmol L-1H2SO4和1mmol L-1 HAuCl4溶液中,静置4min使Au3+与Cu2+发生置换反应,然后去离子水将电极表面清洗干净。重复进行Cu的欠电位沉积,然后将电极快速置于50mmol L-1 H2SO4和1mmol L-1 K2PtCl4混合溶液中,静置4min使Pt2+与Cu2+发生置换反应,然后用去离子水将电极清洗干净即可得到Pt/Au/PdCo/C催化剂。Disperse 5 mg of alloyed PdCo/C catalyst in 2 mL of ethanol, and add 30 μL of 5% Nafion emulsion as a binder. After ultrasonic dispersion for 15 min, 20 μL of the slurry was pipetted and coated on the surface of a glassy carbon electrode as a working electrode. The working electrode was placed in a mixed solution of 50mmol L -1 H 2 SO 4 and 50mmol L -1 CuSO 4 for Cu underpotential deposition: first, the deposition potential of 390mV was maintained for 40s to cause underpotential deposition of Cu on the surface of PdCo nanoparticles, and then Quickly immerse the electrode in a solution of 50mmol L -1 H 2 SO 4 and 1mmol L -1 HAuCl 4 , let it stand for 4 minutes to allow the substitution reaction between Au 3+ and Cu 2+ , and then clean the surface of the electrode with deionized water. The underpotential deposition of Cu was repeated, and then the electrode was quickly placed in the mixed solution of 50mmol L -1 H 2 SO 4 and 1mmol L -1 K 2 PtCl 4 , and stood for 4min to allow the substitution reaction between Pt 2+ and Cu 2+ , Then the electrode is cleaned with deionized water to obtain the Pt/Au/PdCo/C catalyst.

实施例8:Embodiment 8:

称取28.2mg PdCl2和9.6mg Co(NO3)2(Pd/Co原子比为3∶1)溶于100mL去离子水中,加入80mg Vulcan XC-72碳粉并超声分散30min。待分散均匀后滴加25mmol L-1柠檬酸钠水溶液25mL,然后在快速搅拌下缓慢滴加80mmol L-1 NaBH4溶液25mL。30min后将得到的产物过滤,大量去离子水洗涤,80℃真空烘箱干燥8h,得到PdCo/C催化剂。将PdCo/C催化剂于400℃、5vol%H2/Ar气氛下热处理2h即可得到合金化的PdCo/C催化剂。Weigh 28.2mg PdCl 2 and 9.6mg Co(NO 3 ) 2 (Pd/Co atomic ratio is 3:1) and dissolve in 100mL deionized water, add 80mg Vulcan XC-72 carbon powder and ultrasonically disperse for 30min. After uniform dispersion, 25mL of 25mmol L -1 sodium citrate aqueous solution was added dropwise, and then 25mL of 80mmol L -1 NaBH 4 solution was slowly added dropwise under rapid stirring. After 30 minutes, the obtained product was filtered, washed with a large amount of deionized water, and dried in a vacuum oven at 80° C. for 8 hours to obtain a PdCo/C catalyst. The alloyed PdCo/C catalyst can be obtained by heat-treating the PdCo/C catalyst at 400° C. for 2 hours under a 5vol% H 2 /Ar atmosphere.

将5mg合金化的PdCo/C催化剂分散于2mL乙醇中,加入30μL 5%Nafion乳液作粘结剂。超声分散15min后移取20μL浆液涂覆于玻碳电极表面作为工作电极。将工作电极置于50mmol L-1 H2SO4和50mmol L-1CuSO4混合溶液中进行Cu-UPD:首先在390mV的沉积电位维持300s进行CU-UPD,然后快速将电极浸入50mmol L-1 H2SO4和1mmol L-1 HAuCl4混合溶液中,静置4min使置换反应进行完全,再用去离子水将电极清洗干净。重复Cu-UPD过程,然后将电极快速置于50mmol L-1 H2SO4和1mmolL-1 K2PtCl4混合溶液中,静置4min使置换反应进行完全,再用去离子水将电极清洗干净即可得到Pt/Au/PdCo/C催化剂。Disperse 5 mg of alloyed PdCo/C catalyst in 2 mL of ethanol, and add 30 μL of 5% Nafion emulsion as a binder. After ultrasonic dispersion for 15 min, 20 μL of the slurry was pipetted and coated on the surface of a glassy carbon electrode as a working electrode. The working electrode was placed in a mixed solution of 50mmol L -1 H 2 SO 4 and 50mmol L -1 CuSO 4 for Cu-UPD: firstly, the deposition potential of 390mV was maintained for 300s for CU-UPD, and then the electrode was quickly immersed in 50mmol L -1 In the mixed solution of H 2 SO 4 and 1 mmol L -1 HAuCl 4 , let stand for 4 minutes to make the replacement reaction complete, and then clean the electrode with deionized water. Repeat the Cu-UPD process, then quickly place the electrode in a mixed solution of 50mmol L -1 H 2 SO 4 and 1mmolL -1 K 2 PtCl 4 , let it stand for 4min to complete the replacement reaction, and then clean the electrode with deionized water The Pt/Au/PdCo/C catalyst can be obtained.

比较例1:合金化的PdCo/C催化剂Comparative Example 1: Alloyed PdCo/C Catalyst

称取28.2mg PdCl2和9.6mg Co(NO3)2(Pd/Co原子比为3∶1)溶于100mL去离子水中,加入80mg Vulcan XC-72碳粉并超声分散30min。待分散均匀后滴加25mmol L-1柠檬酸钠水溶液25mL,然后在快速搅拌下缓慢滴加80mmol L-1 NaBH4溶液25mL。30min后将得到的产物过滤,大量去离子水洗涤,80℃真空烘箱干燥8h,得到PdCo/C催化剂。Weigh 28.2mg PdCl 2 and 9.6mg Co(NO 3 ) 2 (Pd/Co atomic ratio is 3:1) and dissolve in 100mL deionized water, add 80mg Vulcan XC-72 carbon powder and ultrasonically disperse for 30min. After uniform dispersion, 25mL of 25mmol L -1 sodium citrate aqueous solution was added dropwise, and then 25mL of 80mmol L -1 NaBH 4 solution was slowly added dropwise under rapid stirring. After 30 minutes, the obtained product was filtered, washed with a large amount of deionized water, and dried in a vacuum oven at 80° C. for 8 hours to obtain a PdCo/C catalyst.

将PdCo/C催化剂进行热处理(400℃,5vol%H2/Ar,2h)即可得到合金化的PdCo/C催化剂。The alloyed PdCo/C catalyst can be obtained by heat-treating the PdCo/C catalyst (400° C., 5vol% H 2 /Ar, 2 h).

比较例2:Pt/PdCo/C催化剂Comparative example 2: Pt/PdCo/C catalyst

将5mg合金化的PdCo/C催化剂分散于2mL乙醇中,加入30μL 5%Nafion乳液作粘结剂。超声分散15min后移取20μL浆液涂覆于玻碳电极表面作为工作电极。将工作电极置于50mmol L-1 H2SO4和50mmol L-1CuSO4溶液中进行Cu-UPD:首先在390mV的沉积电位维持120s进行Cu-UPD,然后将电极快速置于50mmol L-1 H2SO4和1mmol L-1 K2PtCl4混合溶液中,静置4min使置换反应进行完全,再用去离子水将电极清洗干净即可得到Pt/PdCo/C催化剂。Disperse 5 mg of alloyed PdCo/C catalyst in 2 mL of ethanol, and add 30 μL of 5% Nafion emulsion as a binder. After ultrasonic dispersion for 15 min, 20 μL of the slurry was pipetted and coated on the surface of a glassy carbon electrode as a working electrode. Place the working electrode in 50mmol L -1 H 2 SO 4 and 50mmol L -1 CuSO 4 solution for Cu-UPD: Firstly, Cu-UPD was performed at a deposition potential of 390mV for 120s, and then the electrode was quickly placed in 50mmol L -1 In the mixed solution of H 2 SO 4 and 1 mmol L -1 K 2 PtCl 4 , let stand for 4 minutes to make the replacement reaction complete, and then clean the electrode with deionized water to obtain the Pt/PdCo/C catalyst.

比较例3:Pt/C催化剂Comparative example 3: Pt/C catalyst

商品20wt.%Pt/C催化剂(E-TEK公司)。Commercial 20wt.% Pt/C catalyst (E-TEK company).

图1是在不同沉积电位下沉积120s,然后以20mV s-1的扫描速率从该电位扫描到820mV得到的Cu溶出曲线,所选电位均高于Cu的体相沉积电位340mV。由图1可见,随着沉积电位的负移,位于470mV和580mV的氧化峰逐渐增大,当沉积电位负移至380mV时开始出现体相沉积Cu的氧化峰,说明Cu在此电位下已经发生体相沉积,因此沉积电位选择为390mV。Figure 1 is the Cu dissolution curve obtained by depositing at different deposition potentials for 120s, and then scanning from this potential to 820mV at a scan rate of 20mV s -1 . The selected potentials are all higher than the bulk deposition potential of Cu, which is 340mV. It can be seen from Figure 1 that as the deposition potential shifts negatively, the oxidation peaks at 470mV and 580mV gradually increase, and when the deposition potential shifts negatively to 380mV, the oxidation peak of Cu in the bulk phase begins to appear, indicating that Cu has already occurred at this potential Bulk phase deposition, so the deposition potential is selected as 390mV.

图2是以390mV为沉积电位,经过不同沉积时间后以20mV s-1的扫描速率从390mV扫描到820mV得到的Cu溶出曲线。由图2可见,随着沉积时间的延长,Cu的阳极溶出峰逐渐增大,到120s后溶出曲线基本重合,说明Cu的欠电位沉积已饱和,随着沉积时间的进一步延长不再有Cu在PdCo表面发生欠电位沉积。UPD过程中这种自我终止的现象源于Cu和贵金属Pd之间的强相互作用,当Pd粒子表面被Cu单层完全包裹之后,Cu无法在Cu原子表面发生欠电位沉积而终止。Figure 2 is the Cu dissolution curve obtained by scanning from 390mV to 820mV at a scan rate of 20mV s -1 after different deposition times with 390mV as the deposition potential. It can be seen from Figure 2 that with the prolongation of the deposition time, the anodic dissolution peak of Cu gradually increases, and the dissolution curves basically coincide after 120 s, indicating that the underpotential deposition of Cu has been saturated, and with the further prolongation of the deposition time, there is no longer Cu in the Underpotential deposition occurs on the PdCo surface. This self-termination phenomenon in the UPD process stems from the strong interaction between Cu and the noble metal Pd. When the surface of Pd particles is completely covered by Cu monolayer, Cu cannot be terminated by underpotential deposition on the surface of Cu atoms.

图3为根据实施例1和比较例2制备得到的样品在0.1M HClO4溶液中的CV曲线和ORR极化曲线。由图3(a)可以看出,同Pt/PdCo/C催化剂相比,Pt/Au/PdCo/C的氢吸脱附峰有所降低,通过积分氢脱附峰计算得到的电化学活性表面积(ECSAs)分别为149.3和144.3m2g-1,如此高的ECSAs可能是由于Pt在催化剂表面高度分散引起的。同时Pt/Au/PdCo/C催化剂中Pt在高电位时的氧化还原峰均有所降低并向高电位移动,说明OH更容易在Pt表面发生吸脱附,预示着ORR催化活性将有所提高。由图3(b)可知,在Pt和PdCo之间引入Au改善了催化剂的ORR催化活性,ORR极化曲线的半波电位由0.878V正移至0.90V,提高了22mV。Fig. 3 is the CV curve and ORR polarization curve of the sample prepared according to Example 1 and Comparative Example 2 in 0.1M HClO 4 solution. It can be seen from Figure 3(a) that compared with the Pt/PdCo/C catalyst, the hydrogen adsorption and desorption peaks of Pt/Au/PdCo/C are reduced, and the electrochemically active surface area calculated by integrating the hydrogen desorption peaks (ECSAs) are 149.3 and 144.3m 2 g -1 , respectively, such high ECSAs may be caused by the highly dispersed Pt on the catalyst surface. At the same time, in the Pt/Au/PdCo/C catalyst, the redox peak of Pt at high potential decreases and moves to high potential, indicating that OH is more likely to be adsorbed and desorbed on the surface of Pt, which indicates that the catalytic activity of ORR will be improved. . It can be seen from Figure 3(b) that the introduction of Au between Pt and PdCo improves the ORR catalytic activity of the catalyst, and the half-wave potential of the ORR polarization curve is positively shifted from 0.878V to 0.90V, which is increased by 22mV.

图4为实施例1和比较例2、3在一定电位下(0.85V和0.9V)单位质量Pt的动力学电流比较。与Pt/C和Pt/PdCo/C催化剂相比,Pt/Au/PdCo/C催化剂在0.85V时ORR催化活性分别提高了13和4倍,大大提高了贵金属Pt的利用率。ORR催化活性的提高可能是由于Au的加入引起Pt晶格收缩,调变了Pt的d带中心,使OH在Pt上更容易脱附。Figure 4 is a comparison of kinetic current per unit mass of Pt in Example 1 and Comparative Examples 2 and 3 at a certain potential (0.85V and 0.9V). Compared with the Pt/C and Pt/PdCo/C catalysts, the Pt/Au/PdCo/C catalyst has 13 and 4 times higher ORR catalytic activity at 0.85 V, respectively, greatly improving the utilization of the noble metal Pt. The enhanced catalytic activity for ORR may be due to the contraction of the Pt lattice caused by the addition of Au, which modulates the d-band center of Pt and makes it easier for OH to desorb on Pt.

图5为根据实施例1和比较例2制备得到的样品在0.1M HClO4溶液中稳定性测试(100mVs-1,0.6-1.0V vs.NHE)前后的CV曲线和ORR极化曲线。由图5可知,经过10k圈CV扫描后,Pt/PdCo/C催化剂的ECSAs和ORR极化曲线半波电位分别下降48.2%和32mV;而经过相同条件的稳定性测试后,Pt/Au/PdCo/C催化剂的ECSAs从144.3降低到104m2g-1,下降27.9%,但ORR催化活性没有明显的衰减,半波电位仅负移13mV。上述结果表明Pt/Au/PdCo/C的稳定性在Pt/PdCo/C的基础上得到了明显的提高。Fig. 5 shows the CV curves and ORR polarization curves of the samples prepared according to Example 1 and Comparative Example 2 before and after the stability test (100mVs -1 , 0.6-1.0V vs. NHE) in 0.1M HClO 4 solution. It can be seen from Figure 5 that after 10k cycles of CV scanning, the half-wave potential of the ECSAs and ORR polarization curves of the Pt/PdCo/C catalyst decreased by 48.2% and 32mV, respectively; and after the stability test under the same conditions, the Pt/Au/PdCo The ECSAs of the /C catalyst decreased from 144.3 to 104m 2 g -1 , decreased by 27.9%, but the ORR catalytic activity did not decline significantly, and the half-wave potential only shifted negatively by 13mV. The above results show that the stability of Pt/Au/PdCo/C has been significantly improved on the basis of Pt/PdCo/C.

图6为根据实施例1和比较例2制备得到的样品在0.1M HClO4溶液中稳定性测试前后的TEM照片。由图6可以看出,在稳定性测试前,Pt/PdCo/C和Pt/Au/PdCo/C催化剂中的纳米粒子都较均匀地分布在炭载体上,平均粒径分别为5.3和5.5nm。经过10k圈CV扫描后,Pt/PdCo/C中的纳米粒子发生严重聚集,且表面变得凹凸不平,催化剂形貌遭到了严重破坏,导致CV曲线中ECSAs和ORR催化活性的大幅度衰减。相比之下,经过同样电化学稳定性测试的Pt/Au/PdCo/C形貌并未发生大的改变,只是纳米粒子粒径略有长大(5.5到6.6nm)。上述结果表明,在Pt和PdCo之间中引入Au次单层后,催化剂的稳定性得到了明显的提高。FIG. 6 is a TEM photo of the samples prepared according to Example 1 and Comparative Example 2 before and after the stability test in 0.1M HClO 4 solution. It can be seen from Figure 6 that before the stability test, the nanoparticles in the Pt/PdCo/C and Pt/Au/PdCo/C catalysts were more uniformly distributed on the carbon support, with average particle sizes of 5.3 and 5.5 nm, respectively. . After 10k cycles of CV scanning, the nanoparticles in Pt/PdCo/C were severely aggregated, and the surface became uneven, and the catalyst morphology was severely damaged, resulting in a large attenuation of the catalytic activity of ECSAs and ORR in the CV curves. In contrast, the morphology of Pt/Au/PdCo/C undergoing the same electrochemical stability test did not change greatly, but the particle size of the nanoparticles increased slightly (5.5 to 6.6nm). The above results indicated that the stability of the catalyst was significantly improved after the introduction of Au submonolayer between Pt and PdCo.

Claims (10)

1. a Pt/Au/PdCo/C catalyst, is characterized in that:
Catalyst is the metal core shell structure that carbon carries, and the metal in catalyst is with PdCo alloy for core, and to be positioned at the Pt on surface for shell, Au is between Pt shell and PdCo core, and in catalyst, Pt is single layer structure, and Au is time single layer structure; In catalyst, metal quality accounts for the 12-46% of gross mass; Wherein the mol ratio of Pd and Co is 5:1-1:1; The mol ratio of Pd and Au is 5:1-12:1; The mol ratio of Pd and Pt is 10:1-20:1; Catalyst adopts the method for Cu-UPD-displacement to be incorporated between surperficial Pt layer and PdCo core as secondary individual layer by Au and prepares.
2. a preparation method for catalyst described in claim 1, is characterized in that: comprise the following steps,
(1) preparation of alloying PdCo/C
A. in deionized water, PdCl is added 2and/or Pd (NO 3) 2, add Co (NO simultaneously 3) 2, CoCl 2, CoBr 2, CoSO 4, Co (COOH) 2in one or more formed mixtures, stir make it to mix, in mixed liquor, add carbon carrier afterwards, and ultrasonic disperse is even to mixed liquor;
B. in above-mentioned steps (1) a gained mixed liquor, drip sodium citrate aqueous solution, and dropwise drip NaBH under the condition stirred 4the aqueous solution, filters to obtain solid matter after leaving standstill, and adopts deionized water to wash gained solid matter afterwards, and it is dry that gained material after washing is placed in vacuum drying oven, obtains PdCo/C;
C. step (1) b gained PdCo/C is heat-treated in hydrogen and inert gas gaseous mixture, obtain alloying PdCo/C;
(2) preparation of Pt/Au/PdCo/C catalyst
A. in ethanol, add above-mentioned steps (1) c gained alloying PdCo/C, stir after making it to mix and add Nafion emulsion, and ultrasonic disperse is even to mixed liquor;
B. pipette above-mentioned steps (2) a gained mixed liquor, and be coated on glassy carbon electrode surface as work electrode, Pt silk is to electrode, and saturated calomel electrode is reference electrode;
C. above-mentioned steps (2) b gained work electrode is placed in H 2sO 4and CuSO 4under the sedimentation potential of 350-520mV, maintain 1-300s in mixed solution, then electrode is immersed H 2sO 4and HAuCl 4also leave standstill 1-10min in mixed solution and carry out displacement reaction, then with deionized water, electrode clean is clean;
D. above-mentioned steps (2) c gained work electrode is placed in H 2sO 4and CuSO 4under the sedimentation potential of 350-520mV, maintain 1-300s in mixed solution, then electrode is immersed H 2sO 4and K 2ptCl 4also leave standstill 1-10min in mixed solution and carry out displacement reaction, then with deionized water, electrode clean is clean, namely obtain Pt/Au/PdCo/C catalyst.
3. the preparation method of catalyst as claimed in claim 2, is characterized in that:
Pd in mixture described in step (1) a 2+and Co 2+mol ratio be 5:1 ~ 1:1; Pd in described mixture 2+concentration be 10-100mmol L -1.
4. the preparation method of catalyst as claimed in claim 2, is characterized in that:
Metal quality in alloying PdCo/C described in step (1) accounts for the 10-40% of gross mass.
5. the preparation method of catalyst as claimed in claim 2, is characterized in that:
Described in step (1) b, the concentration of sodium citrate aqueous solution is 10-50mmol L -1, consumption is 10-50mL; Described NaBH 4the concentration of the aqueous solution is 10-100mmol L -1, consumption is 10-50mL; The described vacuumize time is 5-20 hour.
6. the preparation method of catalyst as claimed in claim 2, is characterized in that:
Inert atmosphere described in step (1) c is the mixture of one or two or more kinds in argon gas, helium, nitrogen; Described hydrogen volume accounts for the 1-10% of volume of gas; Described heat treatment temperature is 200-600 DEG C; Described heat treatment time is 1-3h.
7. the preparation method of catalyst as claimed in claim 2, is characterized in that:
Described in step (2) a, the concentration of PdCo/C in ethanol is 0.5-5mg mL -1; The mass ratio of described Nafion and PdCo/C is 1:10-1:1.
8. the preparation method of catalyst as claimed in claim 2, is characterized in that:
H described in step (2) c and step (2) d 2sO 4and CuSO 4in mixed solution, the thing mass ratio of the two is 5:1-1:2; Described H 2sO 4and HAuCl 4in mixed solution, the thing mass ratio of the two is 100:1-20:1; Described H 2sO 4and K 2ptCl 4in mixed solution, the thing mass ratio of the two is 100:1-20:1; H in above-mentioned three kinds of mixed solutions 2sO 4concentration be 20-100mmol L -1.
9. the preparation method of catalyst as claimed in claim 2, is characterized in that:
Described carbon carrier is: one or more the mixture in XC-72R, BP2000, acetylene black, carbon nano-tube, graphite.
10. an application for Pt/Au/PdCo/C catalyst described in claim 1, is characterized in that: described Pt/Au/PdCo/C catalyst can be used as metal air fuel cell oxygen reduction catalyst, Proton Exchange Membrane Fuel Cells oxygen reduction catalyst or direct liquid fuel battery oxygen reduction catalyst.
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