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CN104218250A - PtM/C electrocatalyst for fuel cell and preparation method of PtM/C electrocatalyst for fuel cell - Google Patents

PtM/C electrocatalyst for fuel cell and preparation method of PtM/C electrocatalyst for fuel cell Download PDF

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CN104218250A
CN104218250A CN201410475946.3A CN201410475946A CN104218250A CN 104218250 A CN104218250 A CN 104218250A CN 201410475946 A CN201410475946 A CN 201410475946A CN 104218250 A CN104218250 A CN 104218250A
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catalyst
fuel cell
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electrocatalyst
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林瑞
范仁杰
杨美妮
赵天天
曾浩
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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
    • H01M4/9075Catalytic material supported on carriers, e.g. powder carriers
    • H01M4/9083Catalytic material supported on carriers, e.g. powder carriers on carbon or graphite
    • 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
    • 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
    • H01M4/96Carbon-based electrodes
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells

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  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
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Abstract

The invention relates to a PtM/C electrocatalyst for a fuel cell. The PtM/C electrocatalyst comprises the following components by mass percent: 18.16-36.52% of active components, 1.74-3.68% of auxiliary agents and the balance being a conductive carrier. The PtM/C electrocatalyst is prepared by the steps of feeding precursors of the active components and precursors of the auxiliary agents into a mixed suspension liquid of the conductive carrier and a reducing agent in one step; loading metal Pt and M onto the conductive carrier by adopting a pulse microwave-assisted chemical reduction method; and after that, precipitating, filtering, washing and carrying out vacuum drying to obtain the PtM/C electrocatalyst. Compared with the prior art, the preparation method is simple; the prepared PtM/C electrocatalyst is uniform in particle distribution, small in size and high in catalytic activity of oxygen reduction reaction, and can be used in the field of the fuel cell.

Description

一种燃料电池用PtM/C电催化剂及其制备方法A kind of PtM/C electrocatalyst for fuel cell and preparation method thereof

技术领域technical field

本发明属于燃料电池技术领域,涉及一种催化剂及其制备方法,尤其是涉及一种燃料电池用PtM/C电催化剂及其制备方法。The invention belongs to the technical field of fuel cells, and relates to a catalyst and a preparation method thereof, in particular to a PtM/C electrocatalyst for a fuel cell and a preparation method thereof.

背景技术Background technique

由于质子交换膜燃料电池(PEMFC)具有能量转化效率高,易启动,对环境污染小等特点,其可以用作电动车辆的动力源、分布式电站以及便携式可移动电源,近年来已受到世界各国的广泛关注,其关键技术也得到了快速发展。Because the proton exchange membrane fuel cell (PEMFC) has the characteristics of high energy conversion efficiency, easy start-up, and low environmental pollution, it can be used as a power source for electric vehicles, a distributed power station, and a portable mobile power source. Its key technologies have also been developed rapidly.

众所周知,催化剂是PEMFC的关键材料,研究开发出活性高、稳定性好的催化剂对提高燃料电池的性能起举足轻重的作用。而为了适合商业化大批量生产,PtM/C催化剂的制备方法有待改进,以往制备PtM/C催化剂多采用浸渍法、液相还原法及胶体法进行制备,然而这几种方法均存在不同程度的技术缺陷。例如,液相还原法一般用还原剂在一定温度下还原催化剂活性组分,然后使其担载在碳载体上,此方法通常采用传统的对流加热,存在加热不均匀及反应速率慢等缺点;浸渍法制备的催化剂粒径大,而且粒度分布均一性差,金属的一次担载量不能太高,需进行多次浸渍;而胶体法制备周期长,而且过程不易控制。As we all know, catalyst is the key material of PEMFC, research and development of catalyst with high activity and good stability plays a decisive role in improving the performance of fuel cell. In order to be suitable for commercial mass production, the preparation method of PtM/C catalyst needs to be improved. In the past, the preparation method of PtM/C catalyst was mostly prepared by impregnation method, liquid phase reduction method and colloid method. However, these methods have different degrees of limitations. technical flaws. For example, the liquid phase reduction method generally uses a reducing agent to reduce the catalyst active component at a certain temperature, and then load it on a carbon carrier. This method usually uses traditional convective heating, which has disadvantages such as uneven heating and slow reaction rate; The catalyst prepared by the impregnation method has a large particle size and poor particle size distribution uniformity. The metal loading capacity cannot be too high at one time, and multiple impregnations are required; while the colloid method has a long preparation period and is difficult to control.

为了提高贵金属的利用率,常将贵金属负载在某些载体上,以提高其分散性。催化剂载体不仅能够对催化剂活性组分起到支撑和分散作用,同时,对催化剂的传质、传热以及化学稳定性和热稳定性等均具有重要作用。导电性碳黑材料是燃料电池催化剂理想的载体选择,因为其具备如下条件:(1)较高的比表面积,能有效地分散贵金属活性组分;(2)高度石墨化,具有良好的电子传导能力;(3)适当的孔结构,以减小反应物、中间体和产物的传输迁移阻力。In order to improve the utilization rate of precious metals, precious metals are often loaded on some carriers to improve their dispersion. The catalyst support can not only support and disperse the active components of the catalyst, but also play an important role in the mass transfer, heat transfer, chemical stability and thermal stability of the catalyst. Conductive carbon black material is an ideal carrier choice for fuel cell catalysts, because it has the following conditions: (1) high specific surface area, which can effectively disperse noble metal active components; (2) highly graphitized, with good electronic conductivity (3) Appropriate pore structure to reduce the transport migration resistance of reactants, intermediates and products.

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颗粒尺寸小、具有较高催化活性的燃料电池用PtM/C电催化剂。The object of the present invention is to provide a PtM/C electrocatalyst for fuel cells with small particle size and high catalytic activity 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:The purpose of the present invention can be achieved through the following technical solutions:

一种燃料电池用PtM/C电催化剂,该PtM/C电催化剂包括以下质量百分比的成分:活性组分18.16~36.52%、助剂M1.74~3.68%,其余为导电性载体。A PtM/C electrocatalyst for a fuel cell. The PtM/C electrocatalyst includes the following components in mass percentage: active component 18.16-36.52%, auxiliary agent M 1.74-3.68%, and the rest is a conductive carrier.

所述的活性组分为金属Pt,所述的助剂M包括Fe、Co、Ni中的一种或几种单质。The active component is metal Pt, and the additive M includes one or several simple substances of Fe, Co, and Ni.

所述的导电性载体包括Vulcan XC-72、乙炔黑、Ketjen黑、碳纳米管、碳纳米角、碳纳米分子筛、石墨纳米纤维、氧化石墨烯及石墨烯中的一种或多种。The conductive carrier includes one or more of Vulcan XC-72, acetylene black, Ketjen black, carbon nanotubes, carbon nanohorns, carbon nanomolecular sieves, graphite nanofibers, graphene oxide and graphene.

一种燃料电池用PtM/C电催化剂的制备方法,该方法是将活性组分前驱体和助剂前驱体一步加入到导电性载体与还原剂的混合悬浮液中,采用脉冲微波辅助化学还原法将金属Pt和M从前驱体中还原,并负载在导电性载体上,再经沉淀、过滤、洗涤、真空干燥,即制得PtM/C电催化剂,具体包括以下步骤:A method for preparing a PtM/C electrocatalyst for a fuel cell, the method is to add the active component precursor and the auxiliary agent precursor to the mixed suspension of the conductive carrier and the reducing agent in one step, and adopt the pulse microwave assisted chemical reduction method The metal Pt and M are reduced from the precursor, and loaded on a conductive carrier, and then precipitated, filtered, washed, and vacuum-dried to obtain a PtM/C electrocatalyst, which specifically includes the following steps:

(1)按导电性载体与还原剂的质量比为1∶(100~600),将导电性载体加入到还原剂溶液中,超声搅拌均匀,制得悬浮液A;(1) According to the mass ratio of the conductive carrier and the reducing agent being 1: (100-600), the conductive carrier is added to the reducing agent solution, and the suspension A is obtained by ultrasonic stirring;

(2)按助剂前驱体中M与活性组分前驱体中Pt的摩尔比为1∶3,将活性组分前驱体和助剂前驱体一起加入到步骤(1)制得的悬浮液A中,超声搅拌均匀,调节溶液pH值为8~12,制得悬浮液B;(2) According to the molar ratio of M in the auxiliary agent precursor and Pt in the active ingredient precursor is 1: 3, the active ingredient precursor and the auxiliary agent precursor are added together to the suspension A prepared in step (1) , ultrasonically stirred evenly, adjusted the pH value of the solution to 8-12, and prepared suspension B;

(3)将步骤(2)制得的悬浮液B置于微波反应器中,采用脉冲微波辅助化学还原法进行反应,反应结束后,待溶液温度降至室温,经沉淀、过滤、洗涤、真空干燥,即制得PtM/C电催化剂。(3) Place the suspension B prepared in step (2) in a microwave reactor, and react by using pulsed microwave-assisted chemical reduction. After drying, the PtM/C electrocatalyst is obtained.

步骤(2)所述的活性组分前驱体与步骤(1)所述的导电性载体的质量比为1∶(1.5~2)。The mass ratio of the active component precursor described in step (2) to the conductive carrier described in step (1) is 1: (1.5-2).

所述的活性组分前驱体包括氯铂酸或硝酸铂。The active component precursor includes chloroplatinic acid or platinum nitrate.

所述的助剂前驱体包括M的可溶性有机盐或可溶性无机盐,所述的M的可溶性无机盐优选硝酸盐、硫酸盐或氯化物,所述的M的可溶性有机盐优选乙酸盐。The auxiliary agent precursor includes a soluble organic salt or a soluble inorganic salt of M, the soluble inorganic salt of M is preferably nitrate, sulfate or chloride, and the soluble organic salt of M is preferably acetate.

所述的还原剂包括甲醛、乙醛、乙二醇、丙三醇及硼氢化钠中的一种或多种。The reducing agent includes one or more of formaldehyde, acetaldehyde, ethylene glycol, glycerol and sodium borohydride.

步骤(3)所述的采用脉冲微波辅助化学还原法的操作条件为:向微波反应器中通入惰性保护气体,微波反应器的工作时间为5~50s,弛豫时间为50~300s,微波功率为0.5~3kW,微波重复作用次数为5~30次。The operation condition of adopting the pulse microwave assisted chemical reduction method described in step (3) is: pass into the inert protective gas in the microwave reactor, the working time of the microwave reactor is 5~50s, the relaxation time is 50~300s, microwave The power is 0.5-3kW, and the number of microwave repetitions is 5-30 times.

步骤(3)所述的真空干燥的温度为60~120℃,真空度为-0.09~-0.1MPa,干燥时间为6~12h。The vacuum drying temperature in step (3) is 60-120°C, the vacuum degree is -0.09--0.1MPa, and the drying time is 6-12h.

与现有技术相比,本发明具有以下特点:Compared with the prior art, the present invention has the following characteristics:

(1)采用脉冲微波辅助化学还原法进行制备,操作方法简单,反应条件温和,反应速率快,能实现将活性组分与助剂一次同时负载于导电性载体上;(1) It is prepared by pulse microwave-assisted chemical reduction method, the operation method is simple, the reaction conditions are mild, the reaction rate is fast, and the active component and auxiliary agent can be loaded on the conductive carrier at one time;

(2)制备所得的PtM/C电催化剂颗粒尺寸小,粒度分布均匀,热稳定性好,具有良好的对氧还原反应催化性能。(2) The prepared PtM/C electrocatalyst has small particle size, uniform particle size distribution, good thermal stability, and good catalytic performance for oxygen reduction reaction.

附图说明Description of drawings

图1为实施例1所制备的PtM/C电催化剂线性扫描伏安测试谱图;Fig. 1 is the PtM/C electrocatalyst linear sweep voltammetry test spectrogram prepared by embodiment 1;

图2为实施例1所制备的PtM/C电催化剂的透射电子显微镜(TEM)谱图;Fig. 2 is the transmission electron microscope (TEM) spectrogram of the PtM/C electrocatalyst prepared by embodiment 1;

图3为实施例2所制备的PtM/C电催化剂线性扫描伏安测试谱图;Fig. 3 is the PtM/C electrocatalyst linear sweep voltammetry test spectrogram prepared by embodiment 2;

图4为实施例2所制备的PtM/C电催化剂的透射电子显微镜(TEM)谱图;Fig. 4 is the transmission electron microscope (TEM) spectrogram of the PtM/C electrocatalyst prepared by embodiment 2;

图5为实施例3所制备的PtM/C电催化剂的循环伏安(CV)谱图;Fig. 5 is the cyclic voltammetry (CV) spectrogram of the PtM/C electrocatalyst prepared by embodiment 3;

图6为实施例3所制备的PtM/C电催化剂线性扫描伏安测试谱图;Fig. 6 is the PtM/C electrocatalyst linear sweep voltammetry test spectrogram prepared by embodiment 3;

图7为实施例4所制备的PtM/C电催化剂线性扫描伏安测试谱图;Fig. 7 is the PtM/C electrocatalyst linear sweep voltammetry test spectrogram prepared by embodiment 4;

图8为实施例4所制备的PtM/C电催化剂的X射线衍射谱图(XRD)。8 is an X-ray diffraction spectrum (XRD) of the PtM/C electrocatalyst prepared in Example 4.

具体实施方式Detailed ways

下面结合附图和具体实施例对本发明进行详细说明。The present invention will be described in detail below in conjunction with the accompanying drawings and specific embodiments.

实施例1:Example 1:

本实施例,采用脉冲微波辅助化学还原法制备Pt3Ni/XC-72电催化剂(Pt与Ni摩尔比3∶1,Pt3Ni占催化剂总质量的百分比为20%,则Pt占催化剂总质量的百分比为18.18%,Ni占催化剂总质量的百分比为1.82%),具体制备方法如下:In this example, the Pt3Ni /XC-72 electrocatalyst was prepared by pulsed microwave-assisted chemical reduction (the molar ratio of Pt to Ni is 3:1, the percentage of Pt3Ni accounting for the total mass of the catalyst is 20%, then Pt accounts for the total mass of the catalyst The percentage of Ni is 18.18%, and the percentage of Ni accounting for the total mass of the catalyst is 1.82%), and the specific preparation method is as follows:

(1)按Vulcan XC-72碳黑(美国Cabot公司)与乙二醇的质量比为1∶200,将Vulcan XC-72加入到乙二醇中,超声搅拌均匀,制得悬浮液A;(1) According to the mass ratio of Vulcan XC-72 carbon black (Cabot, USA) to ethylene glycol is 1:200, add Vulcan XC-72 to ethylene glycol, and stir evenly with ultrasonic to prepare suspension A;

(2)按硝酸镍中Ni与氯铂酸中Pt的摩尔比为1∶3,将氯铂酸与硝酸镍一起加入到步骤(1)制得的悬浮液A中,其中,氯铂酸与Vulcan XC-72的质量比控制为1∶1.66,超声搅拌均匀,调节溶液pH值为10,制得悬浮液B;(2) by the mol ratio of Ni in nickel nitrate and Pt in chloroplatinic acid is 1: 3, chloroplatinic acid and nickel nitrate are joined in the suspension A that step (1) makes together, wherein, chloroplatinic acid and The mass ratio of Vulcan XC-72 was controlled to be 1:1.66, stirred evenly by ultrasonic, and the pH value of the solution was adjusted to 10 to prepare suspension B;

(3)将步骤(2)制得的悬浮液B置于微波反应器中,通入惰性气体氮气,排尽空气,设置微波反应器的工作时间为20s,弛豫时间为100s,微波功率为1kW,微波重复作用次数为15次,启动微波反应器,进行还原反应;待反应结束后,将溶液温度降至室温,取出溶液经沉淀、过滤、洗涤,得到样品,并将样品在80℃、真空度为-0.1MPa,真空干燥8h,即制备得到Pt3Ni/XC-72电催化剂。(3) Suspension B that step (2) is made is placed in microwave reactor, feeds inert gas nitrogen, exhausts air, and the operating time of setting microwave reactor is 20s, and relaxation time is 100s, and microwave power is 1kW, the number of microwave repetitions is 15 times, start the microwave reactor, and carry out the reduction reaction; after the reaction is completed, the temperature of the solution is lowered to room temperature, the solution is taken out, precipitated, filtered, and washed to obtain a sample, and the sample is placed at 80 ° C, The degree of vacuum is -0.1MPa, and vacuum drying is carried out for 8 hours to prepare the Pt 3 Ni/XC-72 electrocatalyst.

将本实施例制备所得的Pt3Ni/XC-72电催化剂进行线性扫描伏安测试,测试条件:扫描范围为0.05~1.2V(vs.RHE),扫描速度为5mV·s-1,电极转速为1600rpm,溶液为氧气饱和的0.1mol·L-1HClO4溶液,测试结果如图1所示。The Pt 3 Ni/XC-72 electrocatalyst prepared in this example was subjected to a linear sweep voltammetry test, the test conditions: the sweep range was 0.05-1.2V (vs. RHE), the sweep speed was 5mV·s -1 , the electrode speed 1600rpm, the solution is 0.1mol·L -1 HClO 4 solution saturated with oxygen, and the test results are shown in Figure 1.

由图1可以看出,制备所得的Pt3Ni/XC-72电催化剂在0.9V电压下的电流密度达到1.1mA/cm2,具有良好的对氧还原催化性能。It can be seen from Figure 1 that the prepared Pt 3 Ni/XC-72 electrocatalyst has a current density of 1.1 mA/cm 2 at a voltage of 0.9 V, and has good catalytic performance for oxygen reduction.

图2所示为本实施例制备所得Pt3Ni/XC-72电催化剂的TEM谱图,由图2可以看出,制备所得的Pt3Ni/XC-72电催化剂的颗粒大小均匀,分散良好,基本没有团结现象,颗粒的平均粒径约为2.5nm。Figure 2 shows the TEM spectrum of the Pt3Ni /XC-72 electrocatalyst prepared in this example. It can be seen from Figure 2 that the prepared Pt3Ni /XC-72 electrocatalyst has uniform particle size and good dispersion , There is basically no unity phenomenon, and the average particle size of the particles is about 2.5nm.

实施例2:Example 2:

本实施例,采用脉冲微波辅助化学还原法制备Pt3Ni/乙炔黑电催化剂(Pt与Ni摩尔比3∶1,Pt3Ni占催化剂总质量的百分比为20%,则Pt占催化剂总质量的百分比为18.18%,Ni占催化剂总质量的百分比为1.82%),具体制备方法如下:In this example, a Pt3Ni /acetylene black electrocatalyst was prepared by pulsed microwave-assisted chemical reduction (the molar ratio of Pt to Ni is 3:1, the percentage of Pt3Ni accounting for the total mass of the catalyst is 20%, and then Pt accounts for 20% of the total mass of the catalyst. Percentage is 18.18%, and the percentage that Ni accounts for catalyst gross mass is 1.82%), and concrete preparation method is as follows:

(1)按乙炔黑(美国Alfa公司)与乙二醇的质量比为1∶200,将乙炔黑加入到乙二醇中,超声搅拌均匀,制得悬浮液A;(1) According to the mass ratio of acetylene black (Alfa, USA) to ethylene glycol is 1: 200, acetylene black is added to ethylene glycol, and ultrasonically stirred evenly to obtain suspension A;

(2)按硝酸镍中Ni与氯铂酸中Pt的摩尔比为1∶3,将氯铂酸与硝酸镍一起加入到步骤(1)制得的悬浮液A中,其中,氯铂酸与乙炔黑的质量比控制为1∶1.66,超声搅拌均匀,调节溶液pH值为10,制得悬浮液B;(2) by the mol ratio of Ni in nickel nitrate and Pt in chloroplatinic acid is 1: 3, chloroplatinic acid and nickel nitrate are joined in the suspension A that step (1) makes together, wherein, chloroplatinic acid and The mass ratio of acetylene black is controlled to be 1:1.66, the ultrasonic stirring is uniform, the pH value of the solution is adjusted to 10, and the suspension B is obtained;

(3)将步骤(4)制得的悬浮液B置于微波反应器中,通入惰性气体氮气排尽空气,设置微波反应器的工作时间为30s,弛豫时间为200s,微波功率为2kW,微波重复作用次数为20次,启动微波反应器,进行还原反应;待反应结束后,将溶液温度降至室温,取出溶液经沉淀、过滤、洗涤,得到样品,并将样品在60℃、真空度为-0.10MPa,真空干燥10h,即制备得到Pt3Ni/乙炔黑电催化剂。(3) Suspension B prepared by step (4) is placed in a microwave reactor, feeds inert gas nitrogen to exhaust the air, the working time of the microwave reactor is set to 30s, the relaxation time is 200s, and the microwave power is 2kW , the number of microwave repetitions is 20 times, the microwave reactor is started, and the reduction reaction is carried out; after the reaction is completed, the temperature of the solution is lowered to room temperature, the solution is taken out, and the sample is obtained by precipitation, filtration, and washing, and the sample is placed at 60 ° C under vacuum The density is -0.10MPa, vacuum drying for 10h, the Pt 3 Ni/acetylene black electrocatalyst is prepared.

将本实施例制备所得的Pt3Ni/乙炔黑电催化剂进行线性扫描伏安测试,测试条件:扫描范围为0.05~1.2V(vs.RHE),扫描速度为5mV·s-1,电极转速为1600rpm,溶液为氧气饱和的0.1mol·L-1HClO4溶液,测试结果如图3所示,Pt3Ni/乙炔黑电催化剂具有良好的对氧还原催化性能。The Pt 3 Ni/acetylene black electrocatalyst prepared in this example was subjected to a linear sweep voltammetry test. The test conditions were: the sweep range was 0.05-1.2V (vs. RHE), the sweep speed was 5mV·s -1 , and the electrode speed was 1600rpm, the solution is 0.1mol·L -1 HClO 4 solution saturated with oxygen, the test results are shown in Figure 3, the Pt 3 Ni/acetylene black electrocatalyst has good catalytic performance for oxygen reduction.

图4所示为本实施例制备所得Pt3Ni/乙炔黑电催化剂的TEM谱图,由图4可以看出,制备所得的Pt3Ni/乙炔黑电催化剂的颗粒大小均匀,分散良好,基本没有团结现象,颗粒的平均粒径约为2.3nm。Figure 4 shows the TEM spectrogram of the Pt3Ni /acetylene black electrocatalyst prepared in this example. As can be seen from Figure 4, the prepared Pt3Ni /acetylene black electrocatalyst has uniform particle size, good dispersion, and basically There is no solidification phenomenon, and the average particle size of the particles is about 2.3nm.

实施例3:Example 3:

本实施例,采用脉冲微波辅助化学还原法制备Pt3Fe/XC-72电催化剂(Pt与Fe摩尔比3∶1,Pt3Fe占催化剂总质量的百分比为20%,则Pt占催化剂总质量的百分比为18.26%,Fe占催化剂总质量的百分比为1.74%),具体制备方法如下:In this example, the Pt 3 Fe/XC-72 electrocatalyst was prepared by pulsed microwave assisted chemical reduction (the molar ratio of Pt to Fe is 3:1, the percentage of Pt 3 Fe in the total mass of the catalyst is 20%, then Pt in the total mass of the catalyst The percentage of Fe is 18.26%, and the percentage of Fe accounting for the total mass of the catalyst is 1.74%), and the specific preparation method is as follows:

(1)按Vulcan XC-72与乙二醇的质量比为1∶300,将Vulcan XC-72加入到乙二醇中,超声搅拌均匀,制得悬浮液A;(1) According to the mass ratio of Vulcan XC-72 and ethylene glycol as 1:300, add Vulcan XC-72 to ethylene glycol, and stir evenly with ultrasonic to prepare suspension A;

(2)按硝酸铁中Fe与氯铂酸中Pt的摩尔比为1∶3,将氯铂酸与硝酸铁一起加入到步骤(1)制得的悬浮液A中,其中,氯铂酸与Vulcan XC-72的质量比控制为1∶1.66,超声搅拌均匀,调节溶液pH值为10,制得悬浮液B;(2) by the molar ratio of Fe in ferric nitrate and Pt in chloroplatinic acid is 1: 3, chloroplatinic acid and ferric nitrate are joined in the suspension A that step (1) makes together, wherein, chloroplatinic acid and The mass ratio of Vulcan XC-72 was controlled at 1:1.66, stirred evenly by ultrasonic, and the pH value of the solution was adjusted to 10 to prepare suspension B;

(3)将步骤(2)制得的悬浮液B置于微波反应器中,通入惰性气体氮气排尽空气,设置微波反应器的工作时间为20s,弛豫时间为100s,微波功率为1kW,微波重复作用次数为15次,启动微波反应器,进行还原反应;待反应结束后,将溶液温度降至室温,取出溶液经沉淀、过滤、洗涤,得到样品,并将样品在80℃、真空度为-0.10MPa,真空干燥8h,即制备得到Pt3Fe/XC-72电催化剂。(3) Suspension B prepared by step (2) is placed in a microwave reactor, and the inert gas nitrogen is introduced to exhaust the air. The working time of the microwave reactor is set to be 20s, the relaxation time is 100s, and the microwave power is 1kW , the number of microwave repetitions is 15 times, the microwave reactor is started, and the reduction reaction is carried out; after the reaction is completed, the temperature of the solution is lowered to room temperature, the solution is taken out, and the sample is obtained by precipitation, filtration, and washing, and the sample is placed at 80 ° C under vacuum The density is -0.10MPa, vacuum drying for 8h, and the Pt 3 Fe/XC-72 electrocatalyst is prepared.

将本实施制备所得的Pt3Fe/XC-72电催化剂进行循环伏安测试,测试条件:扫描范围为0.05~1.15V(vs.RHE),扫描速率为50mV·s-1,测试曲线如图5所示。The Pt 3 Fe/XC-72 electrocatalyst prepared in this practice was subjected to cyclic voltammetry test, the test conditions: the scan range was 0.05-1.15V (vs.RHE), the scan rate was 50mV·s -1 , and the test curve was shown in the figure 5.

由图5可计算得知,制备所得的Pt3Fe/XC-72电催化剂的电化学活性面积达到83m2/g,具有较大的活性面积。It can be calculated from Fig. 5 that the electrochemically active area of the prepared Pt 3 Fe/XC-72 electrocatalyst reaches 83m 2 /g, which has a relatively large active area.

将本实施例制备所得的Pt3Fe/XC-72电催化剂进行线性扫描伏安测试,测试条件:扫描范围为0.05~1.2V(vs.RHE),扫描速度为5mV·s-1,电极转速为1600rpm,溶液为氧气饱和的0.1mol·L-1HClO4溶液,测试结果如图6所示,可以看出,制备所得的Pt3Fe/XC-72电催化剂在0.9V电压下的电流密度达到1.2mA/cm2,具有良好的对氧还原催化性能。The Pt 3 Fe/XC-72 electrocatalyst prepared in this example was subjected to a linear sweep voltammetry test. The test conditions were: the sweep range was 0.05-1.2V (vs. RHE), the sweep speed was 5mV·s -1 , the electrode rotational speed is 1600rpm, and the solution is a 0.1mol L -1 HClO 4 solution saturated with oxygen. The test results are shown in Figure 6. It can be seen that the current density of the prepared Pt 3 Fe/XC-72 electrocatalyst at a voltage of 0.9V Reaching 1.2mA/cm 2 , it has good catalytic performance for oxygen reduction.

实施例4:Example 4:

本实施例,采用脉冲微波辅助化学还原法制备Pt3Ni/GO电催化剂(Pt与Ni摩尔比3∶1,Pt3Ni占催化剂总质量的百分比为20%,则Pt占催化剂总质量的百分比为18.18%,Ni占催化剂总质量的百分比为1.82%),其中GO为氧化石墨烯(南京先丰纳米材料科技公司),具体制备方法如下:In this example, the Pt 3 Ni/GO electrocatalyst was prepared by pulsed microwave-assisted chemical reduction (the molar ratio of Pt to Ni is 3:1, the percentage of Pt 3 Ni in the total mass of the catalyst is 20%, and the percentage of Pt in the total mass of the catalyst is is 18.18%, and the percentage of Ni accounting for the total mass of the catalyst is 1.82%), wherein GO is graphene oxide (Nanjing Xianfeng Nano Material Technology Co., Ltd.), and the specific preparation method is as follows:

(1)按氧化石墨烯与丙三醇的质量比为1∶200,将氧化石墨烯加入到丙三醇中,超声搅拌均匀,制得悬浮液A;(1) According to the mass ratio of graphene oxide and glycerol is 1: 200, graphene oxide is added in glycerin, ultrasonic stirring is even, obtained suspension A;

(2)按硝酸镍中Ni与氯铂酸中Pt的摩尔比为1∶3,将氯铂酸与硝酸镍一起加入到步骤(1)制得的悬浮液A中,其中,氯铂酸与氧化石墨烯的质量比控制为1∶1.66,超声搅拌均匀,调节溶液pH值为10,制得悬浮液B;(2) by the mol ratio of Ni in nickel nitrate and Pt in chloroplatinic acid is 1: 3, chloroplatinic acid and nickel nitrate are joined in the suspension A that step (1) makes together, wherein, chloroplatinic acid and The mass ratio of graphene oxide is controlled to be 1: 1.66, the ultrasonic stirring is uniform, the pH value of the solution is adjusted to 10, and the suspension B is obtained;

(3)将步骤(2)制得的悬浮液B置于微波反应器中,通入惰性气体氮气排尽空气,设置微波反应器的工作时间为20s,弛豫时间为100s,微波功率为1kW,微波重复作用次数为15次,启动微波反应器,进行还原反应;待反应结束后,将溶液温度降至室温,取出溶液经沉淀、过滤、洗涤,得到样品,并将样品在80℃、真空度为-0.10MPa,真空干燥8h,即制备得到Pt3Ni/GO电催化剂。(3) Suspension B prepared by step (2) is placed in a microwave reactor, and the inert gas nitrogen is introduced to exhaust the air. The working time of the microwave reactor is set to be 20s, the relaxation time is 100s, and the microwave power is 1kW , the number of microwave repetitions is 15 times, the microwave reactor is started, and the reduction reaction is carried out; after the reaction is completed, the temperature of the solution is lowered to room temperature, the solution is taken out, and the sample is obtained by precipitation, filtration, and washing, and the sample is placed at 80 ° C under vacuum The temperature was -0.10MPa, and vacuum drying was carried out for 8 hours to prepare the Pt 3 Ni/GO electrocatalyst.

将本实施例制备所得的Pt3Ni/GO电催化剂进行线性扫描伏安测试,测试条件:扫描范围为0.05-1.2V(vs.RHE),扫描速度为5mV·s-1,电极转速为1600rpm,溶液为氧气饱和的0.1mol·L-1HClO4溶液,测试结果如图7所示,可以看出,制备所得的Pt3Ni/GO电催化剂在0.9V电压下的电流密度达到1.0mA/cm2,具有良好的对氧还原催化性能。The Pt 3 Ni/GO electrocatalyst prepared in this example was subjected to a linear sweep voltammetry test, the test conditions: the sweep range was 0.05-1.2V (vs. RHE), the sweep speed was 5mV·s -1 , and the electrode speed was 1600rpm , the solution is 0.1mol·L -1 HClO 4 solution saturated with oxygen. The test results are shown in Figure 7. It can be seen that the current density of the prepared Pt 3 Ni/GO electrocatalyst at 0.9V voltage reaches 1.0mA/ cm 2 , has good catalytic performance for oxygen reduction.

图8为本实施制备所得Pt3Ni/GO电催化剂的XRD测试谱图,测试条件:工作压力为40kV,扫描范围为20°-90°,扫描速度为6°/min。Figure 8 is the XRD test spectrum of the Pt 3 Ni/GO electrocatalyst prepared in this practice. The test conditions are: the working pressure is 40kV, the scanning range is 20°-90°, and the scanning speed is 6°/min.

图8中第一个峰出现在20=25°为C(002),Pt(111)、Pt(200)、Pt(220)、Pt(311)分别对应的2θ角值为40°、46°、68°、81°,其中Pt(111)的峰最强,说明制得的Pt3Ni/GO电催化剂中Pt颗粒主要为面心立方晶型。In Figure 8, the first peak appears at 20=25°, which is C(002), and the corresponding 2θ angle values of Pt(111), Pt(200), Pt(220), and Pt(311) are 40° and 46° respectively , 68°, 81°, among which the Pt(111) peak is the strongest, indicating that the Pt particles in the prepared Pt 3 Ni/GO electrocatalyst are mainly in the face-centered cubic crystal form.

实施例5:Example 5:

本实施例,采用脉冲微波辅助化学还原法制备Pt3Fe/碳纳米管(中科院成都有机所)电催化剂(Pt与Fe摩尔比3∶1,Pt3Fe占催化剂总质量的百分比为40%,则Pt占催化剂总质量的百分比为36.52%,Fe占催化剂总质量的百分比为3.48%),具体制备方法如下:In this example, a Pt 3 Fe/carbon nanotube (Chengdu Institute of Organic Chemistry, Chinese Academy of Sciences) electrocatalyst (Pt to Fe molar ratio 3:1, Pt 3 Fe accounting for 40% of the total mass of the catalyst was prepared by pulsed microwave assisted chemical reduction method, Then the percentage of Pt accounting for the total mass of the catalyst is 36.52%, and the percentage of Fe accounting for the total mass of the catalyst is 3.48%), and the specific preparation method is as follows:

(1)按碳纳米管与乙二醇的质量比为1∶600,将碳纳米管加入到乙二醇中,超声搅拌均匀,制得悬浮液A;(1) According to the mass ratio of carbon nanotubes and ethylene glycol as 1:600, carbon nanotubes are added to ethylene glycol, and ultrasonically stirred evenly to prepare suspension A;

(2)按硝酸铁中Fe与硝酸铂中Pt的摩尔比为1∶3,将硝酸铂和硝酸铁一起加入到步骤(1)制得的悬浮液A中,其中,硝酸铂与碳纳米管的质量比控制为1∶1.5,超声搅拌均匀,调节溶液pH值为8,制得悬浮液B;(2) According to the molar ratio of Fe in ferric nitrate and Pt in platinum nitrate as 1: 3, platinum nitrate and ferric nitrate are added together in the suspension A that step (1) makes, wherein, platinum nitrate and carbon nanotube The mass ratio of the solution is controlled to be 1:1.5, and the ultrasonic stirring is uniform, and the pH value of the solution is adjusted to be 8 to obtain a suspension B;

(3)将步骤(2)制得的悬浮液B置于微波反应器中,通入惰性气体氮气排尽空气,设置微波反应器的工作时间为50s,弛豫时间为300s,微波功率为0.5kW,微波重复作用次数为5次,启动微波反应器,进行还原反应;待反应结束后,将溶液温度降至室温,取出溶液经沉淀、过滤、洗涤,得到样品,并将样品在120℃、真空度为-0.09MPa,真空干燥6h,即制备得到Pt3Fe/碳纳米管电催化剂。(3) Suspension B prepared by step (2) is placed in a microwave reactor, and the inert gas nitrogen is introduced to exhaust the air. The working time of the microwave reactor is set to be 50s, the relaxation time is 300s, and the microwave power is 0.5 kW, the number of microwave repetitions is 5 times, start the microwave reactor, and carry out the reduction reaction; The degree of vacuum is -0.09MPa, and vacuum drying is carried out for 6 hours to prepare a Pt 3 Fe/carbon nanotube electrocatalyst.

实施例6:Embodiment 6:

本实施例,采用脉冲微波辅助化学还原法制备Pt3Co/乙炔黑电催化剂(Pt与Co摩尔比3∶1,Pt3Co占催化剂总质量的百分比为20%,则Pt占催化剂总质量的百分比为18.16%,Co占催化剂总质量的百分比为1.84%),具体制备方法如下:In this embodiment, a Pt 3 Co/acetylene black electrocatalyst was prepared by pulsed microwave assisted chemical reduction (the molar ratio of Pt to Co is 3:1, the percentage of Pt 3 Co in the total mass of the catalyst is 20%, and the percentage of Pt in the total mass of the catalyst is Percentage is 18.16%, and the percentage of Co accounting for the total mass of catalyst is 1.84%), and concrete preparation method is as follows:

(1)按乙炔黑与乙二醇的质量比为1∶300,将乙炔黑加入到乙二醇中,超声搅拌均匀,制得悬浮液A;(1) According to the mass ratio of acetylene black and ethylene glycol as 1:300, acetylene black is added to ethylene glycol, and ultrasonically stirred to obtain a suspension A;

(2)按硝酸钴中Co与硝酸铂中Pt的摩尔比为1∶3,将硝酸铂和硝酸钴一起加入到步骤(1)制得的悬浮液A中,其中,硝酸铂与乙炔黑的质量比控制为11.8,超声搅拌均匀,调节溶液pH值为10,制得悬浮液B;(2) The molar ratio of Co in cobalt nitrate and Pt in platinum nitrate is 1: 3, platinum nitrate and cobalt nitrate are added in the suspension A that step (1) makes together, wherein, platinum nitrate and acetylene black The mass ratio is controlled to be 1 : 1.8, and the ultrasonic stirring is uniform, and the pH value of the solution is adjusted to be 10, and the suspension B is obtained;

(3)将步骤(2)制得的悬浮液B置于微波反应器中,通入惰性气体氮气排尽空气,设置微波反应器的工作时间为5s,弛豫时间为50s,微波功率为3kW,微波重复作用次数为30次,启动微波反应器,进行还原反应;待反应结束后,将溶液温度降至室温,取出溶液经沉淀、过滤、洗涤,得到样品,并将样品在60℃、真空度为-0.10MPa,真空干燥12h,即制备得到Pt3Co/乙炔黑电催化剂。(3) Suspension B prepared by step (2) is placed in a microwave reactor, and the inert gas nitrogen is introduced to exhaust the air. The working time of the microwave reactor is set to be 5s, the relaxation time is 50s, and the microwave power is 3kW , the number of microwave repetitions is 30 times, the microwave reactor is started, and the reduction reaction is carried out; after the reaction is completed, the temperature of the solution is lowered to room temperature, the solution is taken out, and the sample is obtained by precipitation, filtration, and washing, and the sample is placed at 60 ° C under vacuum The density is -0.10MPa, vacuum drying for 12h, and the Pt 3 Co/acetylene black electrocatalyst is prepared.

实施例7:Embodiment 7:

本实施例,采用脉冲微波辅助化学还原法制备Pt3Co/碳纳米管电催化剂(Pt与Co摩尔比3∶1,Pt3Co占催化剂总质量的百分比为40%,则Pt占催化剂总质量的百分比为36.32%,Co占催化剂总质量的百分比为3.68%),具体制备方法如下:In this example, a Pt 3 Co/carbon nanotube electrocatalyst was prepared by pulsed microwave-assisted chemical reduction (the molar ratio of Pt to Co is 3:1, and the percentage of Pt 3 Co in the total mass of the catalyst is 40%, then Pt in the total mass of the catalyst The percentage of is 36.32%, and the percentage of Co accounting for the total mass of the catalyst is 3.68%), and the specific preparation method is as follows:

(1)按碳纳米管与乙二醇的质量比为1∶100,将碳纳米管加入到乙二醇中,超声搅拌均匀,制得悬浮液A;(1) According to the mass ratio of carbon nanotubes and ethylene glycol as 1:100, carbon nanotubes are added to ethylene glycol, and ultrasonically stirred evenly to prepare suspension A;

(2)按硝酸钴中Co与硝酸铂中Pt的摩尔比为1∶3,将硝酸铂与硝酸钴一起加入到步骤(1)制得的悬浮液A中,其中,硝酸铂与碳纳米管的质量比控制为1∶2,超声搅拌均匀,调节溶液pH值为12,制得悬浮液B;(2) According to the molar ratio of Co in cobalt nitrate and Pt in platinum nitrate is 1: 3, platinum nitrate and cobalt nitrate are added in the suspension A that step (1) makes together, wherein, platinum nitrate and carbon nanotube The mass ratio of the solution is controlled to be 1:2, the ultrasonic stirring is uniform, the pH value of the solution is adjusted to 12, and the suspension B is obtained;

(3)将步骤(2)制得的悬浮液B置于微波反应器中,通入惰性气体氮气排尽空气,设置微波反应器的工作时间为25s,弛豫时间为150s,微波功率为1.5kW,微波重复作用次数为30次,启动微波反应器,进行还原反应;待反应结束后,将溶液温度降至室温,取出溶液经沉淀、过滤、洗涤,得到样品,并将样品在100℃、真空度为-0.09MPa,真空干燥10h,即制备得到Pt3Co/碳纳米管电催化剂。(3) Suspension B prepared by step (2) is placed in a microwave reactor, feeds inert gas nitrogen to exhaust the air, the working time of the microwave reactor is set to 25s, the relaxation time is 150s, and the microwave power is 1.5 kW, the number of microwave repetitions is 30 times, start the microwave reactor, and carry out the reduction reaction; The vacuum degree is -0.09MPa, and vacuum drying is carried out for 10 hours to prepare the Pt 3 Co/carbon nanotube electrocatalyst.

Claims (10)

1. a fuel cell PtM/C eelctro-catalyst, is characterized in that, this PtM/C eelctro-catalyst comprises the composition of following mass percent: active component 18.16~36.52%, auxiliary agent M1.74~3.68%, all the other are conductive carrier.
2. a kind of fuel cell PtM/C eelctro-catalyst according to claim 1, is characterized in that, described active component is Pt metal, and described auxiliary agent M comprises one or more simple substance in Fe, Co, Ni.
3. a kind of fuel cell PtM/C eelctro-catalyst according to claim 1, it is characterized in that, described conductive carrier comprises that Vulcan XC-72, acetylene black, Ketjen are black, one or more in carbon nano-tube, carbon nanohorn, carbon nano molecular sieve, gnf, graphene oxide and Graphene.
4. the preparation method of PtM/C eelctro-catalyst for a fuel cell as claimed in claim 1, it is characterized in that, the method is that active component presoma and auxiliary agent presoma one step are joined in the mixing suspension of conductive carrier and reducing agent, adopt pulse microwave assistant chemical reducing process that Pt metal and M are reduced from presoma, and load in conductive carrier, through precipitation, filtration, washing, vacuumize, make PtM/C eelctro-catalyst again, specifically comprise the following steps:
(1) by the mass ratio of conductive carrier and reducing agent, be 1: (100~600), conductive carrier is joined in reductant solution, ultrasonic agitation is even, makes suspending liquid A;
(2) by the mol ratio of Pt in M in auxiliary agent presoma and active component presoma, it is 1: 3, active component presoma is joined together with auxiliary agent presoma in the suspending liquid A that step (1) makes, ultrasonic agitation is even, and regulator solution pH value is 8~12, makes suspension B;
(3) suspension B step (2) being made is placed in microwave reactor, adopt pulse microwave assistant chemical reducing process to react, after reaction finishes, treat that solution temperature is down to room temperature, through precipitation, filtration, washing, vacuumize, make PtM/C eelctro-catalyst.
5. the preparation method of PtM/C eelctro-catalyst for a kind of fuel cell according to claim 4, it is characterized in that, the mass ratio of the conductive carrier that the active component presoma that step (2) is described and step (1) are described is 1: (1.5~2).
6. the preparation method of PtM/C eelctro-catalyst for a kind of fuel cell according to claim 4, is characterized in that, described active component presoma comprises chloroplatinic acid or platinum nitrate.
7. according to a kind of fuel cell described in claim 3 or 4, use the preparation method of PtM/C eelctro-catalyst, it is characterized in that, described auxiliary agent presoma comprises solubility organic salt or the soluble inorganic salt of M, the soluble inorganic salt of described M comprises nitrate, sulfate or chloride, and the solubility organic salt of described M comprises acetate.
8. the preparation method of PtM/C eelctro-catalyst for a kind of fuel cell according to claim 4, is characterized in that, described reducing agent comprises one or more in formaldehyde, acetaldehyde, ethylene glycol, glycerol and sodium borohydride.
9. the preparation method of PtM/C eelctro-catalyst for a kind of fuel cell according to claim 4; it is characterized in that; the operating condition of the employing pulse microwave assistant chemical reducing process that step (3) is described is: in microwave reactor, pass into inert protective gas; the operating time of microwave reactor is 5~50s; relaxation time is 50~300s; microwave power is 0.5~3kW, and microwave repeat function number of times is 5~30 times.
10. the preparation method of PtM/C eelctro-catalyst for a kind of fuel cell according to claim 4, is characterized in that, the described vacuum drying temperature of step (3) is 60~120 ℃, and vacuum degree is-0.09~-0.1MPa, and be 6~12h drying time.
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