CN114628700A - Preparation method of platinum-nickel-gold alloy nano catalyst - Google Patents
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Abstract
本发明公开了铂镍金合金纳米催化剂的制备方法。该方法包括以下步骤:(1)配制金属离子混合液:将氯铂酸、氯金酸和镍盐溶于水,调节pH值至9以上;(2)配制炭黑浆料:将炭黑分散于水和乙二醇的混合溶液中;(3)将金属离子混合液加入炭黑浆料中,混匀,加热反应,产物过滤洗涤干燥;(4)将步骤(3)得到的产物分散于水和乙醇的混合溶液中,加入镍盐,混匀后浓缩干燥,得到固体;(5)将步骤(4)得到的固体先用氢气高温还原,再用高氯酸溶液洗涤,得到铂镍金合金纳米催化剂。与现有技术相比,本发明方法操作简单,可规模化生产制备均匀负载的铂镍金合金纳米催化剂,所制备的催化剂具有良好的电催化活性。
The invention discloses a preparation method of platinum-nickel-gold alloy nano-catalyst. The method includes the following steps: (1) preparing a mixed solution of metal ions: dissolving chloroplatinic acid, chloroauric acid and nickel salt in water, and adjusting the pH value to above 9; (2) preparing carbon black slurry: dispersing the carbon black in the mixed solution of water and ethylene glycol; (3) adding the metal ion mixed solution to the carbon black slurry, mixing, heating and reacting, the product is filtered, washed and dried; (4) the product obtained in step (3) is dispersed in In the mixed solution of water and ethanol, nickel salt is added, and after mixing, concentration and drying are performed to obtain a solid; (5) the solid obtained in step (4) is first reduced with hydrogen at high temperature, and then washed with a perchloric acid solution to obtain platinum-nickel-gold Alloy nanocatalysts. Compared with the prior art, the method of the present invention is simple to operate, can produce and prepare uniformly loaded platinum-nickel-gold alloy nano-catalysts on a large scale, and the prepared catalyst has good electrocatalytic activity.
Description
技术领域technical field
本发明属于质子交换膜燃料电池用催化剂领域,具体涉及铂镍金合金纳米催化剂的制备方法。The invention belongs to the field of catalysts for proton exchange membrane fuel cells, in particular to a preparation method of platinum-nickel-gold alloy nano-catalysts.
背景技术Background technique
质子交换膜燃料电池以氢能作为燃料,具有体积小、重量轻、能量转化效率高、无环境污染、原料来源广泛、续航里程长的优点,有广阔的应用前景,被认为是最具有商业价值的燃料电池。Proton exchange membrane fuel cells use hydrogen energy as fuel. They have the advantages of small size, light weight, high energy conversion efficiency, no environmental pollution, wide source of raw materials, and long cruising range. They have broad application prospects and are considered to have the most commercial value. of fuel cells.
质子交换膜燃料电池主要由膜电极、端板、流场板和外电路组成。其中,膜电极由气体扩散层、催化剂和质子交换膜组成,是燃料电池的核心部件。电极反应也在此处发生。电池的两级反应式如下:The proton exchange membrane fuel cell is mainly composed of membrane electrodes, end plates, flow field plates and external circuits. Among them, the membrane electrode is composed of a gas diffusion layer, a catalyst and a proton exchange membrane, and is the core component of the fuel cell. Electrode reactions also take place here. The two-stage reaction of the battery is as follows:
阳极反应:H2→2H++2e- Anodic reaction: H 2 → 2H + +2e -
阴极反应:4H++4e-+O2→2H2OCathodic reaction: 4H + +4e - +O 2 → 2H 2 O
总反应:2H2+O2→2H2OOverall reaction: 2H 2 +O 2 → 2H 2 O
这个反应是自发反应,但反应速率极慢,受到反应动力学的限制,需要使用铂、钯等贵金属作为催化剂来改善动力学性能。然而目前使用的铂催化剂成本高,限制了质子交换膜燃料电池的商业发展。因此,研制更高活性的催化剂是促进质子交换膜燃料电池商业应用的关键步骤。This reaction is a spontaneous reaction, but the reaction rate is extremely slow, which is limited by the reaction kinetics. It is necessary to use noble metals such as platinum and palladium as catalysts to improve the kinetic performance. However, the high cost of platinum catalysts currently used limits the commercial development of proton exchange membrane fuel cells. Therefore, the development of catalysts with higher activity is a key step to promote the commercial application of proton exchange membrane fuel cells.
传统的商用Pt/C催化剂成本高、长期运行导致催化剂团聚长大、碳载体在高温高酸的工作环境下发生腐蚀、质子交换膜的化学降解等一系列问题制约了质子交换膜燃料电池的商业化应用,其中,催化剂本身成本高是制约质子交换膜燃料电池发展的主要因素。将一些相对廉价的过渡金属引入纯铂催化剂形成合金能相对降低铂的使用量,而且能够调整铂的电子结构,降低d带中心,提高催化剂的电催化活性。在合金催化剂中掺入高稳定性的金金属,可提高催化剂的稳定性。但复杂的合金动力学以及Au与其它贵金属(如:Pt,Ru,Rh)或过渡族金属(如:Fe,Co,Ni)的体相热力学不相容性,使得PtAuM(M=Fe,Co,Ni)三元合金材料的构建极具挑战。A series of problems such as high cost of traditional commercial Pt/C catalysts, long-term operation leading to catalyst agglomeration, corrosion of carbon supports in high temperature and high acid working environment, and chemical degradation of proton exchange membranes restrict the commercialization of proton exchange membrane fuel cells. Chemical applications, in which the high cost of the catalyst itself is the main factor restricting the development of proton exchange membrane fuel cells. The introduction of some relatively inexpensive transition metals into pure platinum catalysts to form alloys can relatively reduce the amount of platinum used, and can adjust the electronic structure of platinum, reduce the d-band center, and improve the electrocatalytic activity of the catalyst. Incorporating high-stability gold metal into the alloy catalyst can improve the stability of the catalyst. However, the complex alloy dynamics and the bulk thermodynamic incompatibility of Au with other noble metals (eg: Pt, Ru, Rh) or transition metals (eg: Fe, Co, Ni) make PtAuM (M=Fe, Co , Ni) ternary alloy materials are extremely challenging to construct.
发明内容SUMMARY OF THE INVENTION
基于上述现有技术,本发明的目的在于提供一中铂镍金合金纳米催化剂的制备方法。Based on the above prior art, the purpose of the present invention is to provide a method for preparing a platinum-nickel-gold alloy nano-catalyst.
为实现上述目的,本发明采用如下技术方案:To achieve the above object, the present invention adopts the following technical solutions:
铂镍金合金纳米催化剂的制备方法,包括以下步骤:The preparation method of platinum-nickel-gold alloy nano-catalyst comprises the following steps:
(1)配制金属离子混合液:将氯铂酸、氯金酸和镍盐溶于水,调节pH值至9以上;(1) Preparation of mixed solution of metal ions: chloroplatinic acid, chloroauric acid and nickel salt are dissolved in water, and the pH value is adjusted to above 9;
(2)配制炭黑浆料:将炭黑分散于水和乙二醇的混合溶液中;(2) Preparation of carbon black slurry: disperse carbon black in a mixed solution of water and ethylene glycol;
(3)将金属离子混合液加入炭黑浆料中,混匀,加热反应,产物过滤洗涤干燥;(3) adding the metal ion mixed solution to the carbon black slurry, mixing, heating and reacting, and the product is filtered, washed and dried;
(4)将步骤(3)得到的产物分散于水和乙醇的混合溶液中,加入镍盐,混匀后浓缩干燥,得到固体;(4) disperse the product obtained in step (3) in a mixed solution of water and ethanol, add nickel salt, and concentrate and dry after mixing to obtain a solid;
(5)将步骤(4)得到的固体先用氢气高温还原,再用高氯酸溶液洗涤,得到铂镍金合金纳米催化剂。(5) the solid obtained in step (4) is first reduced with hydrogen at high temperature, and then washed with a perchloric acid solution to obtain a platinum-nickel-gold alloy nano-catalyst.
优选地,所述铂镍金合金纳米催化剂的Pt载量为40wt%以上。Preferably, the Pt loading of the platinum-nickel-gold alloy nanocatalyst is more than 40wt%.
更优选地,Pt载量为40wt%~50wt%。More preferably, the Pt loading is 40wt% to 50wt%.
优选地,步骤(1)中,金属离子混合液中氯铂酸的浓度为1~3wt%。Preferably, in step (1), the concentration of chloroplatinic acid in the metal ion mixed solution is 1-3 wt%.
优选地,氯铂酸、氯金酸和镍盐按Pt、Ni、Au原子比为3:2~6:0.1~1.5投料。其中,步骤(1)投入2/3的镍盐,步骤(4)投入剩余的镍盐。Preferably, chloroplatinic acid, chloroauric acid and nickel salt are charged according to the atomic ratio of Pt, Ni and Au of 3:2-6:0.1-1.5. Wherein, in step (1), 2/3 of the nickel salt is put in, and in step (4) the remaining nickel salt is put in.
步骤(1)加入镍盐的目的是使得镍与铂一同在乙二醇溶液中被还原;步骤(4)加入镍盐的目的是在高温还原过程中抑制铂镍金合金颗粒长大,从而提高催化剂活性。The purpose of adding nickel salt in step (1) is to make nickel and platinum be reduced together in ethylene glycol solution; the purpose of adding nickel salt in step (4) is to suppress the growth of platinum-nickel-gold alloy particles in the high-temperature reduction process, thereby improving the catalyst activity.
更优选地,Pt、Ni、Au原子比为3:3:0.1。More preferably, the atomic ratio of Pt, Ni, Au is 3:3:0.1.
优选地,所述镍盐为硝酸镍或氯化镍。Preferably, the nickel salt is nickel nitrate or nickel chloride.
优选地,步骤(2)中,水和乙二醇的质量比为0.1~1:1,炭黑的浓度为0.1~1wt%。乙二醇即是溶剂,又是还原剂。Preferably, in step (2), the mass ratio of water and ethylene glycol is 0.1-1:1, and the concentration of carbon black is 0.1-1 wt%. Ethylene glycol is both a solvent and a reducing agent.
更优选地,水和乙二醇的质量比为0.3~0.4:1,炭黑的浓度为0.4~0.5wt%。More preferably, the mass ratio of water and ethylene glycol is 0.3-0.4:1, and the concentration of carbon black is 0.4-0.5 wt%.
优选地,步骤(3)中,采用微波反应器加热反应,温度为180~190℃,时间3~10min。采用微波反应器可增加成核速率、缩短反应时间,可以很好的辅助制备催化剂。Preferably, in step (3), a microwave reactor is used to heat the reaction, the temperature is 180-190° C., and the time is 3-10 min. The use of microwave reactor can increase the nucleation rate and shorten the reaction time, which can be a good auxiliary for the preparation of catalysts.
步骤(3)得到的产物在水和乙醇混合溶液中能获得良好的分散性,优选地,水和乙醇的质量比为0.5~3:5,更优选地,水和乙醇的质量比为1~2:5。The product obtained in step (3) can obtain good dispersibility in the mixed solution of water and ethanol, preferably, the mass ratio of water and ethanol is 0.5~3:5, more preferably, the mass ratio of water and ethanol is 1~ 2:5.
优选地,步骤(5)中,氢气高温还原的温度为600~800℃,时间为1~3h。Preferably, in step (5), the temperature of hydrogen high-temperature reduction is 600-800° C., and the time is 1-3 h.
高温还原后,会有部分Ni未能与Pt形成合金,用高氯酸溶液洗涤则起到将这部分未合金化的Ni溶解去掉的作用。After high temperature reduction, some Ni fails to form an alloy with Pt, and washing with perchloric acid solution plays a role in dissolving and removing this part of unalloyed Ni.
有益效果beneficial effect
与现有技术相比,本发明方法操作简单,可规模化生产制备均匀负载有序的铂镍金合金纳米催化剂,所制备的催化剂具有良好的电催化活性。Compared with the prior art, the method of the invention is simple to operate, and can produce and prepare platinum-nickel-gold alloy nano-catalysts with uniform loading and order on a large scale, and the prepared catalyst has good electrocatalytic activity.
附图说明Description of drawings
图1为Pt3Ni3Au0.1/C的XRD图谱与Pt的PDF卡片;Figure 1 is the XRD pattern of Pt 3 Ni 3 Au 0.1 /C and the PDF card of Pt;
图2为Pt3Ni3Au0.1/C的循环伏安图;Fig. 2 is the cyclic voltammogram of Pt 3 Ni 3 Au 0.1 /C;
图3为Pt3Ni3Au0.1/C的半电池线性扫描图。FIG. 3 is a linear scan diagram of a half-cell of Pt 3 Ni 3 Au 0.1 /C.
图4为Pt3Ni3Au0.1/C的透射电镜(TEM)图。FIG. 4 is a transmission electron microscope (TEM) image of Pt 3 Ni 3 Au 0.1 /C.
具体实施方式Detailed ways
以下结合附图及实施例对本发明的技术方案做进一步详细。The technical solutions of the present invention will be further detailed below in conjunction with the accompanying drawings and embodiments.
铂镍金合金纳米催化剂的制备过程如下:The preparation process of platinum-nickel-gold alloy nanocatalyst is as follows:
将氯铂酸水溶液、氯金酸水溶液和三分之二的硝酸镍溶于水中超声分散10-20min;加入适量NaOH溶液,调节pH值到9,得到金属离子混合液,氯铂酸浓度为2wt%;Dissolve chloroplatinic acid aqueous solution, chloroauric acid aqueous solution and two-thirds of nickel nitrate in water for ultrasonic dispersion for 10-20 min; add an appropriate amount of NaOH solution, adjust the pH value to 9, and obtain a metal ion mixed solution, and the concentration of chloroplatinic acid is 2wt %;
将炭黑ECP-600超声均匀分散到水和乙二醇质量比为0.37:1的混合溶液中,超声分散20min,得到炭黑浆料,炭黑浓度为0.45wt%;The carbon black ECP-600 was ultrasonically dispersed uniformly into a mixed solution with a mass ratio of water and ethylene glycol of 0.37:1, and ultrasonically dispersed for 20 min to obtain a carbon black slurry with a carbon black concentration of 0.45wt%;
将上述金属离子混合液逐滴滴入炭黑浆料中,超声分散至均匀,得到前驱液,其中,氯铂酸中铂的质量与炭黑ECP-600的质量比为1:1;The above-mentioned metal ion mixed solution is dropped dropwise into the carbon black slurry, and ultrasonically dispersed to uniformity to obtain a precursor solution, wherein the mass ratio of platinum in the chloroplatinic acid to the mass of carbon black ECP-600 is 1:1;
将前驱液放入微波反应器加热至186℃,反应5min,冷却至90℃取出,过滤洗涤干燥;The precursor solution was put into a microwave reactor and heated to 186 °C, reacted for 5 min, cooled to 90 °C, taken out, filtered, washed and dried;
将干燥后的样品在水和乙醇质量比为1:5的混合溶液中超声分散20min,加入剩余的Ni(NO3)2超声分散1h,在水浴中70℃下蒸至光滑稠状,取出后置于60℃下烘干过夜,得到黑色固体;The dried samples were ultrasonically dispersed in a mixed solution with a mass ratio of water and ethanol of 1:5 for 20 min, and the remaining Ni(NO 3 ) 2 was added to ultrasonically disperse for 1 h, and steamed at 70°C in a water bath until smooth and thick. Dry at 60°C overnight to obtain a black solid;
将黑色固体研磨后置于高温管式炉中(升温速度5℃/min),使用5vol.%的氢氮混合气进行还原(温度700℃,时间2h),得到PtNiAu催化剂粗品;The black solid was ground and placed in a high temperature tube furnace (heating rate 5°C/min), and 5 vol.% hydrogen-nitrogen mixture was used for reduction (temperature 700°C, time 2h) to obtain a crude PtNiAu catalyst;
取0.1g催化剂粗品放入25mL 0.1mol·L-1的高氯酸溶液中,60℃油浴2h,过滤洗涤干燥,得到炭载PtNiAu催化剂,从TEM图可以看出,炭黑上负载的PtNiAu合金分布均匀有序。Take 0.1 g of the crude catalyst and put it into 25 mL of 0.1 mol·L -1 perchloric acid solution, oil bath at 60 °C for 2 h, filter, wash and dry to obtain a carbon-supported PtNiAu catalyst. It can be seen from the TEM image that the PtNiAu supported on carbon black Alloy distribution is uniform and orderly.
通过调整投料时的Pt、Ni、Au原子比,确定Pt、Ni、Au的投料原子比为3:3:0.1时催化剂(ICP测得的Pt实际载量为47.8wt%)的ECSA(电化学活性面积)、MA(氧还原质量比活性)最高,其XRD如图1所示,TEM图如图4所示。By adjusting the atomic ratios of Pt, Ni, and Au during feeding, the ECSA (electrochemical Active area) and MA (oxygen reduction mass specific activity) are the highest, the XRD is shown in Figure 1, and the TEM image is shown in Figure 4.
ECSA通过测定循环伏安曲线计算,MA通过测定半电池线性扫描曲线计算。ECSA was calculated by measuring the cyclic voltammetry curve and MA was calculated by measuring the half-cell linear sweep curve.
ICP测得的Pt3Ni3Au0.1/C催化剂金属成分Catalyst metal composition of Pt 3 Ni 3 Au 0.1 /C measured by ICP
最后应说明的是:以上所述仅为本发明的优选实施例而已,并不用于限制本发明,尽管参照前述实施例对本发明进行了详细的说明,对于本领域的技术人员来说,其依然可以对前述各实施例所记载的技术方案进行修改,或者对其中部分技术特征进行等同替换。凡在本发明的精神和原则之内,所作的任何修改、等同替换、改进等,均应包含在本发明的保护范围之内。Finally, it should be noted that the above are only preferred embodiments of the present invention, and are not intended to limit the present invention. Although the present invention has been described in detail with reference to the foregoing embodiments, for those skilled in the art, it is still The technical solutions described in the foregoing embodiments may be modified, or some technical features thereof may be equivalently replaced. Any modification, equivalent replacement, improvement, etc. made within the spirit and principle of the present invention shall be included within the protection scope of the present invention.
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