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CN108736031A - A kind of self-supporting PtCo alloy nanoparticle catalyst and the preparation method and application thereof - Google Patents

A kind of self-supporting PtCo alloy nanoparticle catalyst and the preparation method and application thereof Download PDF

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CN108736031A
CN108736031A CN201810489697.1A CN201810489697A CN108736031A CN 108736031 A CN108736031 A CN 108736031A CN 201810489697 A CN201810489697 A CN 201810489697A CN 108736031 A CN108736031 A CN 108736031A
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程传伟
任伟娜
张海峰
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Tongji University
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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
    • H01M4/90Selection of catalytic material
    • H01M4/92Metals of platinum group
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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
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    • H01M4/885Impregnation followed by reduction of the catalyst salt precursor
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
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    • H01M4/90Selection of catalytic material
    • H01M4/92Metals of platinum group
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    • H01M4/926Metals of platinum group supported on carriers, e.g. powder carriers on carbon or graphite
    • HELECTRICITY
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    • H01M8/10Fuel cells with solid electrolytes
    • H01M8/1009Fuel cells with solid electrolytes with one of the reactants being liquid, solid or liquid-charged
    • H01M8/1011Direct alcohol fuel cells [DAFC], e.g. direct methanol fuel cells [DMFC]
    • 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
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    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells

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Abstract

本发明涉及一种自支撑PtCo合金纳米颗粒催化剂及其制备方法与应用,具体方法是通过液相手段在碳布上合成三维自支撑钴基金属有机框架(Co‑MOFs)纳米棒阵列结构,经过高温碳热还原技术获得一种三维多孔氮掺杂碳包覆金属钴纳米颗粒(Co@N‑C)纳米棒结构,并以此作为模板,利用金属Pt和Co氧化还原电势的差异,采用简易的电位置换反应方法最终获得了氮掺杂碳/PtCo(PtCo@N‑C)多孔催化剂。与现有技术相比,本发明的复合催化剂无需粘结剂和导电添加剂,具有优异的甲醇氧化性能和CO抗毒性,柔性碳布基底作为集流体,可弯曲可折叠,具有非常好的机械性能。

The invention relates to a self-supporting PtCo alloy nanoparticle catalyst and its preparation method and application. The specific method is to synthesize a three-dimensional self-supporting cobalt-based metal-organic framework (Co-MOFs) nanorod array structure on a carbon cloth by means of a liquid phase. A three-dimensional porous nitrogen-doped carbon-coated metal cobalt nanoparticle (Co@N‑C) nanorod structure was obtained by high-temperature carbothermal reduction technology, and this was used as a template to utilize the difference in the redox potential of metal Pt and Co by simple Nitrogen-doped carbon/PtCo (PtCo@N‑C) porous catalyst was finally obtained by the electroporation reaction method. Compared with the prior art, the composite catalyst of the present invention does not require binders and conductive additives, and has excellent methanol oxidation performance and CO toxicity resistance. The flexible carbon cloth substrate is used as a current collector, which is bendable and foldable, and has very good mechanical properties .

Description

一种自支撑PtCo合金纳米颗粒催化剂及其制备方法与应用A kind of self-supporting PtCo alloy nanoparticle catalyst and its preparation method and application

技术领域technical field

本发明涉及燃料电池技术领域,具体涉及一种自支撑PtCo合金纳米颗粒催化剂及其制备方法与应用。The invention relates to the technical field of fuel cells, in particular to a self-supporting PtCo alloy nanoparticle catalyst and a preparation method and application thereof.

背景技术Background technique

燃料电池作为一种高效的能量转换装置,具有低成本和零排放的潜力,被认为是解决人类日益增长的能源危机和环境污染问题的重要途径。而甲醇具有商业化程度高,比能量高,便携性好等优势,因此,直接甲醇燃料电池具有非常有前途的应用前景并引起了人们的广泛关注。在众多电催化剂当中,铂以及铂基合金仍然是甲醇氧化中最有效和最稳定的催化剂,然而,铂储量有限,价格昂贵,大大的限制了其大规模商业应用。此外,铂的催化性能还受限于其较慢的甲醇氧化动力学以及CO中毒。As a high-efficiency energy conversion device, fuel cells have the potential of low cost and zero emission, and are considered to be an important way to solve human's growing energy crisis and environmental pollution problems. However, methanol has the advantages of high commercialization, high specific energy, and good portability. Therefore, direct methanol fuel cells have very promising application prospects and have attracted widespread attention. Among many electrocatalysts, platinum and platinum-based alloys are still the most effective and stable catalysts in methanol oxidation. However, the limited reserves and high price of platinum greatly limit its large-scale commercial application. In addition, the catalytic performance of platinum is also limited by its slow methanol oxidation kinetics and CO poisoning.

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催化活性好、抗毒能力强且机械性能好的自支撑PtCo合金纳米颗粒催化剂及其制备方法与应用。The purpose of the present invention is to provide a self-supporting PtCo alloy nanoparticle catalyst with good catalytic activity, strong anti-toxicity and good mechanical properties and its preparation method and application in order 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:一种自支撑PtCo合金纳米颗粒催化剂,该催化剂包括三维多孔氮掺杂碳以及包覆在三维多孔氮掺杂碳内部的Pt和Co,其中,所述Pt和Co的质量比为(0.5~0.6):1所述Pt和Co总质量占催化剂质量的43%~48%,所述的三维多孔氮掺杂碳呈阵列结构。本发明采用Pt和Co共同作为催化剂的有效成分,Pt与Co的结合降低了Pt中的电子结合能,促进了低电位下的C-H裂解反应,从而提高了催化剂的活性及抗毒性。同时,由于钴基金属有机框架材料前驱体是三维阵列结构,所以煅烧后多孔氮掺杂碳也是阵列结构。高石墨化多孔氮掺杂碳纳米棒阵列具有大比表面积和高电导率,为PtCO纳米粒子的分散提供了理想的支撑,有利于促进离子/质子的迁移;掺杂的氮元素可增强合金颗粒与碳之间的相互作用,提高催化剂的稳定性;而且多孔氮掺杂碳的本征催化能力对提高的催化活性也做出一定的贡献。The purpose of the present invention can be achieved through the following technical solutions: a self-supporting PtCo alloy nanoparticle catalyst, the catalyst includes three-dimensional porous nitrogen-doped carbon and Pt and Co coated inside the three-dimensional porous nitrogen-doped carbon, wherein, the The mass ratio of Pt and Co is (0.5-0.6): 1. The total mass of Pt and Co accounts for 43%-48% of the mass of the catalyst, and the three-dimensional porous nitrogen-doped carbon has an array structure. The invention adopts Pt and Co together as active components of the catalyst, the combination of Pt and Co reduces the electron binding energy in the Pt, promotes the C-H cracking reaction at low potential, thereby improving the activity and toxicity resistance of the catalyst. At the same time, since the cobalt-based metal organic framework material precursor has a three-dimensional array structure, the porous nitrogen-doped carbon after calcination is also an array structure. The highly graphitized porous nitrogen-doped carbon nanorod array has a large specific surface area and high electrical conductivity, which provides an ideal support for the dispersion of PtCO nanoparticles and facilitates the migration of ions/protons; the doped nitrogen element can strengthen the alloy particles The interaction with carbon improves the stability of the catalyst; and the intrinsic catalytic ability of porous nitrogen-doped carbon also makes a certain contribution to the improved catalytic activity.

一种如上所述自支撑PtCo合金纳米颗粒催化剂的制备方法,包括以下步骤:A method for preparing the self-supporting PtCo alloy nanoparticle catalyst as described above, comprising the following steps:

(1)将碳布放入丙酮的水溶液中进行超声处理,洗涤干燥,然后置于前驱体溶液中,形成钴基金属有机框架化物,其中,所述前驱体溶液为硝酸钴和二甲基咪唑的混合水溶液;(1) Put the carbon cloth into an aqueous solution of acetone for ultrasonic treatment, wash and dry, and then place it in a precursor solution to form a cobalt-based metal organic framework, wherein the precursor solution is cobalt nitrate and dimethylimidazole mixed aqueous solution;

(2)将钴基金属有机框架化物煅烧,得到包覆Co纳米颗粒的三维多孔氮掺杂碳;(2) calcining the cobalt-based metal-organic framework to obtain a three-dimensional porous nitrogen-doped carbon coated with Co nanoparticles;

(3)将得到的包覆Co纳米颗粒的三维多孔氮掺杂碳浸泡在H2PtCl4Pt溶液中,即得所述自支撑PtCo合金纳米颗粒催化剂。(3) Soak the obtained three-dimensional porous nitrogen-doped carbon coated with Co nanoparticles in H 2 PtCl 4 Pt solution to obtain the self-supporting PtCo alloy nanoparticle catalyst.

由于碳纤维编制成的碳布是一种很好的三维导电衬底材料,它的作用一方面可以增加所制备材料的导电性比表面积,有利于增加活性位点;另一方面生长在碳布上的活性材料可直接作为催化电极,省去像其它粉末催化剂那样制成电极的步骤。在整个制备过程中Co由外向内逐渐被Pt取代,形成合金颗粒。Since the carbon cloth made of carbon fiber is a good three-dimensional conductive substrate material, its function can increase the conductivity specific surface area of the prepared material on the one hand, which is beneficial to increase the active sites; on the other hand, it grows on the carbon cloth. The active material can be directly used as a catalytic electrode, eliminating the need to make electrodes like other powder catalysts. During the whole preparation process, Co is gradually replaced by Pt from outside to inside to form alloy particles.

所述的碳布在丙酮的水溶液进行超声处理的时间为20~30min,超声用于清洗碳布。The carbon cloth is ultrasonically treated in an aqueous solution of acetone for 20 to 30 minutes, and the ultrasonic wave is used to clean the carbon cloth.

所述洗涤采用去离子水,干燥温度为60~80℃。The washing uses deionized water, and the drying temperature is 60-80°C.

所述前驱体溶液中,硝酸钴和二甲基咪唑的摩尔比为1:(15~20)。In the precursor solution, the molar ratio of cobalt nitrate and dimethylimidazole is 1:(15-20).

所述煅烧在Ar和H2的混合氛围中进行,其中,其中,Ar占Ar和H2总体积的90%~95%。H2的加入可在煅烧过程中促进Co的催化作用,阵列结构表面长出一些碳纳米管,增大结构的比表面积。The calcination is carried out in a mixed atmosphere of Ar and H 2 , wherein Ar accounts for 90% to 95% of the total volume of Ar and H 2 . The addition of H 2 can promote the catalytic effect of Co during the calcination process, and some carbon nanotubes grow on the surface of the array structure, which increases the specific surface area of the structure.

以小于5℃/min升温到700~900℃,并保温2~4h后,自然降到室温。700~900℃可以使钴基金属有机框架阵列高度石墨化,增加导电性。Raise the temperature to 700-900°C at less than 5°C/min, keep it warm for 2-4 hours, and then cool down to room temperature naturally. 700-900°C can make the cobalt-based metal-organic framework array highly graphitized and increase the conductivity.

所述H2PtCl4Pt溶液的浓度为0.5~2mmol/L,包覆Co纳米颗粒的三维多孔氮掺杂碳在H2PtCl4Pt溶液中浸泡时间为2~4min。The concentration of the H 2 PtCl 4 Pt solution is 0.5-2 mmol/L, and the soaking time of the three-dimensional porous nitrogen-doped carbon coated with Co nanoparticles in the H 2 PtCl 4 Pt solution is 2-4 minutes.

一种如上所述自支撑PtCo合金纳米颗粒催化剂的应用,该催化剂用于甲醇燃料电池的阳极。甲醇燃料电池阳极发生甲醇氧化反应,阴极发生氧还原反应。本发明制备的材料是甲醇氧化催化剂,所以用于甲醇燃料电池的阳极。An application of the self-supporting PtCo alloy nanoparticle catalyst as described above, the catalyst is used in the anode of methanol fuel cell. Methanol oxidation reaction occurs at the anode of the methanol fuel cell, and oxygen reduction reaction occurs at the cathode. The material prepared by the invention is a methanol oxidation catalyst, so it is used for the anode of the methanol fuel cell.

与现有技术相比,本发明的有益效果体现在以下几方面:Compared with the prior art, the beneficial effects of the present invention are reflected in the following aspects:

(1)该催化剂用于甲醇燃料电池的阳极时,甲醇氧化初始电位高,阳极电流密度大;(1) When the catalyst is used in the anode of a methanol fuel cell, the methanol oxidation initial potential is high and the anode current density is large;

(2)该催化剂用于甲醇燃料电池的阳极时,CO抗毒性和耐久性优良。(2) When the catalyst is used in the anode of a methanol fuel cell, it has excellent CO toxicity resistance and durability.

附图说明Description of drawings

图1为三维多孔Co@N-C扫描电镜图片;Figure 1 is a three-dimensional porous Co@N-C scanning electron microscope image;

图2为三维PtCo@N-C催化剂平面扫描电镜图片;Figure 2 is a three-dimensional PtCo@N-C catalyst plane scanning electron microscope picture;

图3为PtCo@N-C和Pt/C在0.5M H2SO4的电解液中以50mV/s的扫速测试的CV曲线。Figure 3 shows the CV curves of PtCo@NC and Pt/C tested at a sweep rate of 50mV/s in 0.5MH 2 SO 4 electrolyte.

图4为PtCo@N-C和Pt/C在0.5M CH3OH+0.5M H2SO4的电解液中以50mV/s的扫速测试的CV曲线。Figure 4 shows the CV curves of PtCo@NC and Pt/C tested at a scan rate of 50mV/s in the electrolyte of 0.5M CH 3 OH+0.5MH 2 SO 4 .

图5为PtCo@N-C和Pt/C在0.5M CH3OH+0.5M H2SO4的电解液中随循环次数增加的峰电流密度对比。Figure 5 is a comparison of the peak current densities of PtCo@NC and Pt/C in the electrolyte of 0.5M CH 3 OH+0.5M H 2 SO 4 with increasing cycle times.

图6为PtCo@N-C和Pt/C在0.5M H2SO4的电解液中测试的CO抗毒性CV曲线。Figure 6 shows the CO anti-toxicity CV curves of PtCo@NC and Pt/C tested in 0.5MH 2 SO 4 electrolyte.

具体实施方式Detailed ways

下面对本发明的实施例作详细说明,本实施例在以本发明技术方案为前提下进行实施,给出了详细的实施方式和具体的操作过程,但本发明的保护范围不限于下述的实施例。The embodiments of the present invention are described in detail below. This embodiment is implemented on the premise of the technical solution of the present invention, and detailed implementation methods and specific operating procedures are provided, but the protection scope of the present invention is not limited to the following implementation example.

实施例1Example 1

一种自支撑PtCo合金纳米颗粒催化剂的制备方法,包括以下步骤:A preparation method of a self-supporting PtCo alloy nanoparticle catalyst, comprising the following steps:

碳布上Co-MOFs纳米棒阵列制备Fabrication of Co-MOFs Nanorod Arrays on Carbon Cloth

首先选用碳布作为基底,型号:WOS1002。将碳布分别放入丙酮和去离子水中超声处理20分钟,最后用去离子水冲洗,放入鼓风干燥箱中进行干燥。First choose carbon cloth as the base, model: WOS1002. The carbon cloth was put into acetone and deionized water for ultrasonic treatment for 20 minutes, and finally rinsed with deionized water and put into a blast drying oven for drying.

配置Co-MOFs前驱体溶液:将40ml 25mM的硝酸钴(Co(NO3)2·6H2O)迅速加入到40ml 0.4M的二甲基咪唑(C4H6N2)水溶液中,然后搅拌。Prepare the Co-MOFs precursor solution: quickly add 40ml 25mM cobalt nitrate (Co(NO 3 ) 2 6H 2 O) to 40ml 0.4M dimethylimidazole (C 4 H 6 N 2 ) aqueous solution, then stir .

在30℃下,将所述处理好的碳布浸泡在所述Co-MOFs前驱体溶液中反应4小时。然后用去离子水冲洗干净。At 30° C., soak the treated carbon cloth in the Co-MOFs precursor solution for 4 hours to react. Then rinse with deionized water.

重复上述步骤,在相同的温度和反应时间下,二次生长Co-MOFs。Repeat the above steps to grow Co-MOFs for the second time under the same temperature and reaction time.

碳布上Co@N-C纳米棒阵列的制备Fabrication of Co@N-C Nanorod Arrays on Carbon Cloth

将所述碳布上制备的Co-MOFs纳米棒阵列,在800℃下,在Ar/H2(5%H2,95%Ar)环境中退火处理2小时,其中,升温速率为5℃/分钟。自然冷却后得到Co@N-C纳米棒阵列结构(图1)。The Co-MOFs nanorod array prepared on the carbon cloth was annealed at 800°C in an Ar/H 2 (5%H 2 , 95%Ar) environment for 2 hours, wherein the heating rate was 5°C/ minute. The Co@NC nanorod array structure was obtained after natural cooling (Fig. 1).

碳布上PtCo@N-C纳米棒阵列的制备Fabrication of PtCo@N-C Nanorod Arrays on Carbon Cloth

将碳布上所述制备好的PtCo@N-C纳米棒阵列放入搅拌着的1mM的氯铂酸(H2PtCl6·6H2O)溶液中浸泡3分钟,标记为PtCo@N-C。反应方程为:The prepared PtCo@NC nanorod array on the carbon cloth was soaked in a stirring 1 mM chloroplatinic acid (H 2 PtCl 6 ·6H 2 O) solution for 3 minutes, which was marked as PtCo@NC. The reaction equation is:

Co+PtCl4 2-→Co2++Pt+4Cl- Co+PtCl 4 2- →Co 2+ +Pt+ 4Cl-

将所述碳布上制备的PtCo@N-C纳米棒阵列,在400℃下,在Ar/H2(5%H2,95%Ar)环境中退火处理1小时,其中,升温速率为3.5℃/分钟。自然冷却后得到PtCo@N-C纳米棒阵列结构(图2)。The PtCo@NC nanorod array prepared on the carbon cloth was annealed at 400°C in an Ar/H 2 (5%H 2 , 95%Ar) environment for 1 hour, wherein the heating rate was 3.5°C/ minute. After natural cooling, the PtCo@NC nanorod array structure was obtained (Fig. 2).

所述制备好的PtCo@N-C中Pt和Co的质量为0.278mg cm-2和0.533mg cm-2,对应的原子数比为14:86。The masses of Pt and Co in the prepared PtCo@NC are 0.278 mg cm -2 and 0.533 mg cm -2 , and the corresponding atomic number ratio is 14:86.

本发明通过液相手段合成了具有大比表面积的三维Co-MOFs纳米棒结构,经过退火处理获得一种Co@N-C结构,以此作为载体,采用简易的Pt前驱体浸泡方法制备了系列Pt负载的PtCo@N-C催化剂,并对催化剂的电催化性能进行了系统测试和分析。The present invention synthesizes a three-dimensional Co-MOFs nanorod structure with a large specific surface area by means of liquid phase, and obtains a Co@N-C structure after annealing treatment, which is used as a carrier, and a series of Pt loads are prepared by using a simple Pt precursor soaking method The PtCo@N-C catalyst, and the electrocatalytic performance of the catalyst was systematically tested and analyzed.

所述制备好的PtCo@N-C催化剂的电催化性能通过电化学工作站在三电极体系下测试。其中,PtCo@N-C催化剂作为工作电极,在饱和KCl溶液中浸泡的Ag/AgCl(+0.197V vsRHE)作为参比电极,石墨棒作为对电极。The electrocatalytic performance of the prepared PtCo@N-C catalyst was tested by an electrochemical workstation under a three-electrode system. Among them, the PtCo@N-C catalyst was used as the working electrode, the Ag/AgCl (+0.197 V vs RHE) soaked in saturated KCl solution was used as the reference electrode, and the graphite rod was used as the counter electrode.

在测量之前,将高纯Ar通入电解液中20分钟,以去除溶液中的CO和O2Before the measurement, high-purity Ar was bubbled into the electrolyte for 20 min to remove CO and O 2 in the solution.

所述制备好的PtCo@N-C催化剂的电化学活性面积通过在0.5M H2SO4的溶液中测试伏安曲线(CV)获得的,其中,测试电压区间为0到1.0V vs RHE,扫速为50mV s-1The electrochemically active area of the prepared PtCo@NC catalyst is obtained by testing the voltammetric curve (CV) in a solution of 0.5MH 2 SO 4 , wherein the test voltage range is 0 to 1.0V vs RHE, and the sweep rate is 50mV s -1 .

所述制备的PtCo@N-C和Pt/C催化剂的电化学活性面积分别为20m2/g和14.2m2/g,PtCo@N-C催化剂展现出更大的电化学活性面积(图3)。The electrochemically active areas of the prepared PtCo@NC and Pt/C catalysts were 20m 2 /g and 14.2m 2 /g, respectively, and the PtCo@NC catalyst exhibited a larger electrochemically active area ( FIG. 3 ).

所述制备好的PtCo@N-C催化剂的甲醇氧化性能通过在包含0.5M H2SO4和0.5MCH3OH的混合溶液中测试伏安曲线(CV)获得的,其中,测试电压区间为0~1.2V vs.RHE,扫速为50mV s-1The methanol oxidation performance of the prepared PtCo@NC catalyst is obtained by testing the voltammetry curve (CV) in a mixed solution containing 0.5MH 2 SO 4 and 0.5MCH 3 OH, wherein the test voltage range is 0-1.2V vs. RHE, the scan rate is 50mV s -1 .

所述制备的PtCo@N-C比Pt/C催化剂具有更负的初始电压(0.563V<0.642V)和更大的正扫峰电流密度(433.5mA mg-1>140mA mg-1)。因此,PtCo@N-C催化剂展现出更优的甲醇氧化活性(图4)。The prepared PtCo@NC has a more negative initial voltage (0.563V<0.642V) and a larger positive sweep current density (433.5mA mg -1 >140mA mg -1 ) than the Pt/C catalyst. Therefore, the PtCo@NC catalyst exhibits better methanol oxidation activity (Fig. 4).

所述制备好的PtCo@N-C催化剂的甲醇氧化稳定性能是在0.5M H2SO4和0.5M CH3OH的混合溶液中测试连续100个循环的CV曲线获得的,其中,测试电压区间为0~1.2Vvs.RHE,扫速为50mV s-1The methanol oxidation stability of the prepared PtCo@NC catalyst is obtained by testing the CV curve of 100 consecutive cycles in a mixed solution of 0.5MH 2 SO 4 and 0.5M CH 3 OH, wherein the test voltage range is 0- 1.2Vvs.RHE, sweep rate is 50mV s -1 .

所述制备的PtCo@N-C和Pt/C催化剂在100个循环之后的阳极峰电流密度保持率分别为峰值的94.4%和68.7%,说明PtCo@N-C催化剂的耐久性由于商业Pt/C(图5)。The anodic peak current density retention rates of the prepared PtCo@N-C and Pt/C catalysts after 100 cycles were 94.4% and 68.7% of the peak values, respectively, indicating that the durability of the PtCo@N-C catalysts is due to the commercial Pt/C (Fig. 5 ).

所述制备好的PtCo@N-C催化剂的CO抗毒性能是在CO饱和的0.5M H2SO4的溶液中测试CV曲线获得的,其中,测试电压区间为-0.1~1.4V vs RHE,扫速为50mV s-1。在测量之前,将高纯CO气和A r气先后通入电解液中各15分钟,以保证催化剂活性位点上覆盖了足够的CO,而溶液中没有CO。The CO anti-poison performance of the prepared PtCo@NC catalyst is obtained by testing the CV curve in a CO-saturated 0.5MH 2 SO 4 solution, wherein the test voltage range is -0.1 to 1.4V vs RHE, and the sweep rate is 50mV s -1 . Before the measurement, high-purity CO gas and Ar gas were passed into the electrolyte for 15 minutes each to ensure that the active sites of the catalyst were covered with enough CO and there was no CO in the solution.

所述制备的PtCo@N-C和Pt/C催化剂的CO解吸附峰分别在0.92V和1.03V处,PtCo@N-C更负的CO解吸附峰证明它具有更优异的CO共溶性(图6)。The CO desorption peaks of the prepared PtCo@N-C and Pt/C catalysts are at 0.92 V and 1.03 V, respectively, and the more negative CO desorption peak of PtCo@N-C proves that it has more excellent CO solubility (Figure 6).

因此,本实施例所制备的PtCo@N-C催化剂具有卓越的甲醇氧化电流密度,CO抗毒性和耐久性。Therefore, the PtCo@N-C catalyst prepared in this example has excellent methanol oxidation current density, CO toxicity resistance and durability.

实施例2Example 2

采用与实施例1类似的制备方法,不同之处在于:Adopt the preparation method similar to embodiment 1, difference is:

(1)碳布在丙酮的水溶液进行超声处理的时间为20min,碳布的干燥温度为60℃;(1) The carbon cloth is ultrasonically treated in an aqueous solution of acetone for 20 minutes, and the drying temperature of the carbon cloth is 60°C;

(2)前驱体溶液中硝酸钴和二甲基咪唑的摩尔比为1:15。(2) The molar ratio of cobalt nitrate and dimethylimidazole in the precursor solution is 1:15.

(3)煅烧在Ar和H2的混合氛围中进行,其中,Ar占总气体体积的90%;煅烧温度为700℃,煅烧时间为4h;(3) The calcination is carried out in a mixed atmosphere of Ar and H 2 , wherein Ar accounts for 90% of the total gas volume; the calcination temperature is 700°C, and the calcination time is 4h;

(4)浸泡所用的H2PtCl4Pt溶液的浓度为0.5m mol/L,浸泡时间为4min。(4) The concentration of the H 2 PtCl 4 Pt solution used for soaking is 0.5mmol/L, and the soaking time is 4min.

上本实施例制备得到的催化剂用在甲醇燃料电池的阳极,经测试发现具有较大的电流密度,并由良好的CO抗毒性能。The catalyst prepared in this example is used in the anode of the methanol fuel cell, and it is found through testing that it has a large current density and has good CO poisoning performance.

实施例3Example 3

采用与实施例1类似的制备方法,不同之处在于:Adopt the preparation method similar to embodiment 1, difference is:

(1)碳布在丙酮的水溶液进行超声处理的时间为30min,碳布的干燥温度为80℃;(1) The carbon cloth is ultrasonically treated in an aqueous solution of acetone for 30 minutes, and the drying temperature of the carbon cloth is 80°C;

(2)前驱体溶液中硝酸钴和二甲基咪唑的摩尔比为1:~20。(2) The molar ratio of cobalt nitrate and dimethylimidazole in the precursor solution is 1:-20.

(3)煅烧在Ar和H2的混合氛围中进行,其中,Ar占总气体体积的90%~95%;煅烧温度为900℃,煅烧时间为2h;(3) The calcination is carried out in a mixed atmosphere of Ar and H 2 , wherein Ar accounts for 90% to 95% of the total gas volume; the calcination temperature is 900°C, and the calcination time is 2h;

(4)浸泡所用的H2PtCl4Pt溶液的浓度为2m mol/L,浸泡时间为2min。(4) The concentration of the H 2 PtCl 4 Pt solution used for soaking is 2mmol/L, and the soaking time is 2min.

上本实施例制备得到的催化剂用在甲醇燃料电池的阳极,经测试发现具有较大的电流密度,并由良好的CO抗毒性能。The catalyst prepared in this example is used in the anode of the methanol fuel cell, and it is found through testing that it has a large current density and has good CO poisoning performance.

Claims (9)

1.一种自支撑PtCo合金纳米颗粒催化剂,其特征在于,该催化剂包括三维多孔氮掺杂碳以及包覆在三维多孔氮掺杂碳内部的Pt和Co,其中,所述Pt和Co的质量比为(0.5~0.6):1所述Pt和Co总质量占催化剂质量的43%~48%,所述的三维多孔氮掺杂碳呈阵列结构。1. A self-supporting PtCo alloy nanoparticle catalyst, characterized in that the catalyst includes three-dimensional porous nitrogen-doped carbon and Pt and Co coated inside the three-dimensional porous nitrogen-doped carbon, wherein the mass of the Pt and Co The ratio is (0.5-0.6): 1. The total mass of Pt and Co accounts for 43%-48% of the mass of the catalyst, and the three-dimensional porous nitrogen-doped carbon has an array structure. 2.一种如权利要求1所述自支撑PtCo合金纳米颗粒催化剂的制备方法,其特征在于,包括以下步骤:2. a preparation method of self-supporting PtCo alloy nanoparticle catalyst as claimed in claim 1, is characterized in that, comprises the following steps: (1)将碳布放入丙酮的水溶液中进行超声处理,洗涤干燥,然后置于前驱体溶液中,形成钴基金属有机框架化物,其中,所述前驱体溶液为硝酸钴和二甲基咪唑的混合水溶液;(1) Put the carbon cloth into an aqueous solution of acetone for ultrasonic treatment, wash and dry, and then place it in a precursor solution to form a cobalt-based metal organic framework, wherein the precursor solution is cobalt nitrate and dimethylimidazole mixed aqueous solution; (2)将钴基金属有机框架化物煅烧,得到包覆Co纳米颗粒的三维多孔氮掺杂碳;(2) calcining the cobalt-based metal-organic framework to obtain a three-dimensional porous nitrogen-doped carbon coated with Co nanoparticles; (3)将得到的包覆Co纳米颗粒的三维多孔氮掺杂碳浸泡在H2PtCl4Pt溶液中,即得所述自支撑PtCo合金纳米颗粒催化剂。(3) Soak the obtained three-dimensional porous nitrogen-doped carbon coated with Co nanoparticles in H 2 PtCl 4 Pt solution to obtain the self-supporting PtCo alloy nanoparticle catalyst. 3.根据权利要求2所述的一种自支撑PtCo合金纳米颗粒催化剂的制备方法,其特征在于,所述的碳布在丙酮的水溶液进行超声处理的时间为20~30min。3 . The method for preparing a self-supporting PtCo alloy nanoparticle catalyst according to claim 2 , wherein the carbon cloth is ultrasonically treated in an aqueous solution of acetone for 20 to 30 minutes. 4 . 4.根据权利要求2所述的一种自支撑PtCo合金纳米颗粒催化剂的制备方法,其特征在于,所述洗涤采用去离子水,干燥温度为60~80℃。4 . The method for preparing a self-supporting PtCo alloy nanoparticle catalyst according to claim 2 , wherein deionized water is used for the washing, and the drying temperature is 60-80° C. 5.根据权利要求2所述的一种自支撑PtCo合金纳米颗粒催化剂的制备方法,其特征在于,所述前驱体溶液中,硝酸钴和二甲基咪唑的摩尔为1:(15~20)。5. the preparation method of a kind of self-supporting PtCo alloy nanoparticle catalyst according to claim 2, is characterized in that, in described precursor solution, the mole of cobalt nitrate and dimethylimidazole is 1:(15~20) . 6.根据权利要求2所述的一种自支撑PtCo合金纳米颗粒催化剂的制备方法,其特征在于,所述煅烧在Ar和H2的混合氛围中进行,其中,Ar占Ar和H2总体积的90%~95%。6. the preparation method of a kind of self-supporting PtCo alloy nanoparticle catalyst according to claim 2, is characterized in that, described calcining is carried out in the mixed atmosphere of Ar and H , wherein, Ar accounts for Ar and H 2 total volume 90% to 95% of that. 7.根据权利要求6所述的一种自支撑PtCo合金纳米颗粒催化剂的制备方法,其特征在于,所述煅烧步骤为:以小于5℃/min升温到700~900℃,并保温2~4h后,自然降到室温。7. The preparation method of a self-supporting PtCo alloy nanoparticle catalyst according to claim 6, characterized in that the calcination step is: heating up to 700-900°C at a rate of less than 5°C/min, and keeping the temperature for 2-4h After that, let it cool down to room temperature naturally. 8.根据权利要求2所述的一种自支撑PtCo合金纳米颗粒催化剂的制备方法,其特征在于,所述H2PtCl4Pt溶液的浓度为0.5~2mmol/L,包覆Co纳米颗粒的三维多孔氮掺杂碳在H2PtCl4Pt溶液中浸泡时间为2~4min。8. The method for preparing a self-supporting PtCo alloy nanoparticle catalyst according to claim 2, wherein the concentration of the H 2 PtCl 4 Pt solution is 0.5 to 2 mmol/L, and the three-dimensional coating of Co nanoparticles The soaking time of the porous nitrogen-doped carbon in the H 2 PtCl 4 Pt solution is 2-4 minutes. 9.一种如权利要求1所述自支撑PtCo合金纳米颗粒催化剂的应用,其特征在于,该催化剂用于甲醇燃料电池的阳极。9. The application of a self-supporting PtCo alloy nanoparticle catalyst as claimed in claim 1, characterized in that the catalyst is used for the anode of a methanol fuel cell.
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CN113948726A (en) * 2021-09-26 2022-01-18 湖北大学 Flexible dual-functional electrocatalyst for zinc-air battery and preparation method thereof
CN114006000A (en) * 2021-11-05 2022-02-01 电子科技大学 A kind of preparation method of anti-SO3H poisoning Pt-based oxygen reduction catalyst
CN114400339A (en) * 2021-12-06 2022-04-26 江苏大学 A heteropolyacid@MOFs/polymer electrospun nanofibers
CN114400339B (en) * 2021-12-06 2023-09-12 江苏大学 heteropolyacid@MOFs/polymer electrostatic spinning nanofiber
CN114373943A (en) * 2021-12-14 2022-04-19 同济大学 A PtCo/C alloy cathode catalyst for vehicle fuel cell and its preparation method and application
CN114373943B (en) * 2021-12-14 2023-11-24 同济大学 PtCo/C alloy cathode catalyst for vehicle-mounted fuel cell and preparation method and application thereof
CN115513436A (en) * 2022-10-13 2022-12-23 西安交通大学苏州研究院 Self-supporting sulfur @ metal particle/nitrogen-doped carbon nano array electrode material with high sulfur loading capacity and preparation method and application thereof
CN116525856A (en) * 2023-03-28 2023-08-01 电子科技大学 Preparation method of Pt-based oxygen reduction reaction catalyst with high stability
CN116364962A (en) * 2023-03-31 2023-06-30 武汉氢能与燃料电池产业技术研究院有限公司 Ordered Pt/bimetallic MOF (metal oxide fuel) based fuel cell catalytic layer and preparation method thereof

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