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CN110270362B - Manganese-nitrogen co-doped molybdenum carbide nanorod and preparation method and application thereof - Google Patents

Manganese-nitrogen co-doped molybdenum carbide nanorod and preparation method and application thereof Download PDF

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CN110270362B
CN110270362B CN201910597196.XA CN201910597196A CN110270362B CN 110270362 B CN110270362 B CN 110270362B CN 201910597196 A CN201910597196 A CN 201910597196A CN 110270362 B CN110270362 B CN 110270362B
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李永生
徐杰宇
周亚君
李亮
李赟恒
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East China University of Science and Technology
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Abstract

本发明涉及一种锰氮共掺杂碳化钼纳米棒的制备方法,包括如下步骤:S1,将钼源、锰盐和苯胺加入水中超声形成混合浊液,其中,锰原子与钼原子的摩尔比为0.001‑0.5∶1,苯胺与钼原子的摩尔比为1‑10∶1;S2,通过加入无机酸调控混合浊液的pH至3‑6,反应得到锰改性的钼胺前驱体;S3,在还原性的煅烧气氛中煅烧锰改性的钼胺前驱体得到锰氮共掺杂碳化钼纳米棒。本发明还提供由上述的制备方法得到的锰氮共掺杂碳化钼纳米棒及其作为电催化剂的应用。根据本发明的锰氮共掺杂碳化钼纳米棒的制备方法,流程简单、产量高、成本低、且易于大规模生产。

Figure 201910597196

The invention relates to a method for preparing a manganese-nitrogen co-doped molybdenum carbide nanorod, comprising the following steps: S1, adding a molybdenum source, a manganese salt and aniline into water to ultrasonically form a mixed turbid liquid, wherein the molar ratio of manganese atoms to molybdenum atoms is is 0.001-0.5:1, and the molar ratio of aniline to molybdenum atom is 1-10:1; S2, by adding inorganic acid to adjust the pH of the mixed turbid liquid to 3-6, the reaction obtains a manganese-modified molybdenum amine precursor; S3 and calcining the manganese-modified molybdenum amine precursor in a reducing calcining atmosphere to obtain manganese-nitrogen co-doped molybdenum carbide nanorods. The present invention also provides the manganese-nitrogen co-doped molybdenum carbide nanorod obtained by the above preparation method and its application as an electrocatalyst. According to the preparation method of the manganese-nitrogen co-doped molybdenum carbide nanorods of the present invention, the process is simple, the yield is high, the cost is low, and the mass production is easy.

Figure 201910597196

Description

一种锰氮共掺杂碳化钼纳米棒及其制备方法和应用A kind of manganese nitrogen co-doped molybdenum carbide nanorod and its preparation method and application

技术领域technical field

本发明涉及电催化制氢,更具体地涉及一种锰氮共掺杂碳化钼纳米棒 及其制备方法和应用。The invention relates to electrocatalytic hydrogen production, and more particularly to a manganese-nitrogen co-doped molybdenum carbide nanorod and a preparation method and application thereof.

背景技术Background technique

以蓬勃发展的可再生能源(如太阳能、风能等)转换的电能分解水制 氢是实现大规模制备高纯氢气的重要方法。目前市场上使用的电解水制氢催 化剂是铂基贵金属催化剂,其产氢性能突出,但同时也存在价格高昂、储量 有限等问题。因此,探索价格低廉、来源丰富、高效的非贵金属制氢催化剂 具有重要的现实意义。Hydrogen production by splitting water with electricity converted from booming renewable energy sources (such as solar energy, wind energy, etc.) is an important method to achieve large-scale production of high-purity hydrogen. The electrolytic water hydrogen production catalyst currently used in the market is a platinum-based precious metal catalyst, which has outstanding hydrogen production performance, but also has problems such as high price and limited reserves. Therefore, it is of great practical significance to explore inexpensive, abundant and efficient non-precious metal catalysts for hydrogen production.

碳化钼作为一种过渡金属碳化物,因其类铂电子结构、高化学稳定性 以及突出的催化性能而受到关注。但是,碳化钼在制备过程中普遍存在颗粒 团聚、表面污染碳覆盖等问题。同时,由于碳化钼中钼原子未占据的d轨道 密度较大,导致催化剂-氢吸附能(ΔGH*)过大,不利于氢气的脱附,析氢动 力学缓慢。Molybdenum carbide, a transition metal carbide, has attracted attention due to its platinum-like electronic structure, high chemical stability, and outstanding catalytic properties. However, in the preparation process of molybdenum carbide, there are common problems such as particle agglomeration and surface contamination carbon coverage. At the same time, due to the high density of d orbitals unoccupied by molybdenum atoms in molybdenum carbide, the catalyst-hydrogen adsorption energy (ΔG H* ) is too large, which is not conducive to the desorption of hydrogen, and the kinetics of hydrogen evolution is slow.

发明内容SUMMARY OF THE INVENTION

为了解决现有技术中的碳化钼纳米棒存在的颗粒团聚、表面覆盖污染 碳且不利于脱附氢气等问题,本发明提供一种锰氮共掺杂碳化钼纳米棒及其 制备方法和应用。In order to solve the problems of particle agglomeration, surface coverage of polluted carbon and unfavorable desorption of hydrogen in the molybdenum carbide nanorods in the prior art, the present invention provides a manganese-nitrogen co-doped molybdenum carbide nanorod and a preparation method and application thereof.

本发明提供一种锰氮共掺杂碳化钼纳米棒的制备方法,包括如下步骤: S1,将钼源、锰盐和苯胺加入水中超声形成混合浊液,其中,锰原子与钼原 子的摩尔比为0.001-0.5∶1,苯胺与钼原子的摩尔比为1-10∶1;S2,通过加入无 机酸调控混合浊液的pH至3-6,反应得到锰改性的钼胺前驱体(又称为MoOx- 胺有机-无机杂化前驱体);S3,在还原性的煅烧气氛中煅烧锰改性的钼胺前驱 体得到锰氮共掺杂碳化钼纳米棒。The present invention provides a method for preparing manganese-nitrogen co-doped molybdenum carbide nanorods, comprising the following steps: S1, adding molybdenum source, manganese salt and aniline into water to ultrasonically form a mixed turbid liquid, wherein the molar ratio of manganese atoms to molybdenum atoms is is 0.001-0.5: 1, and the molar ratio of aniline to molybdenum atom is 1-10: 1; S2, by adding inorganic acid, the pH of the mixed turbid liquid is regulated to 3-6, and the reaction obtains a manganese-modified molybdenum amine precursor (also It is called MoO x - amine organic-inorganic hybrid precursor); S3, calcining manganese-modified molybdenum amine precursor in a reducing calcining atmosphere to obtain manganese-nitrogen co-doped molybdenum carbide nanorods.

本发明通过锰氮元素共掺杂来优化碳化钼电子结构,降低催化剂-氢吸 附能,加速碳化钼析氢动力学,提高电解水析氢活性。具体地,以锰改性的 钼胺作前驱体,调控前驱体配料中Mn、Mo的元素配比,在还原气氛中煅烧 得到锰氮共掺杂碳化钼纳米棒电催化剂。根据本发明的制备方法得到的锰氮 共掺杂碳化钼纳米棒在拉曼光谱、高倍透射电镜照片中,均不含碳的特征峰、 晶格条纹,表明其表面不含污染碳;同时电感耦合等离子体发射光谱、X射 线光电子能谱等证明Mn、N元素的存在。总之,根据本发明的制备方法流程 简单、经济合理,易于实现大规模生产。The invention optimizes the electronic structure of molybdenum carbide by co-doping with manganese and nitrogen elements, reduces the catalyst-hydrogen adsorption energy, accelerates the kinetics of hydrogen evolution of molybdenum carbide, and improves the hydrogen evolution activity of electrolyzed water. Specifically, using manganese-modified molybdenum amine as a precursor, regulating the element ratio of Mn and Mo in the precursor ingredients, and calcining in a reducing atmosphere to obtain a manganese-nitrogen co-doped molybdenum carbide nanorod electrocatalyst. The manganese-nitrogen co-doped molybdenum carbide nanorods obtained by the preparation method of the present invention do not contain characteristic peaks and lattice fringes of carbon in Raman spectra and high-power transmission electron microscope photos, indicating that their surfaces do not contain polluted carbon; Coupled plasma emission spectroscopy, X-ray photoelectron spectroscopy, etc. proved the existence of Mn and N elements. In a word, the preparation method according to the present invention is simple, economical and reasonable, and is easy to realize large-scale production.

优选地,在所述步骤S1中,将钼源和锰盐超声溶于水中,加入苯胺作 为碳源。Preferably, in the step S1, the molybdenum source and the manganese salt are ultrasonically dissolved in water, and aniline is added as the carbon source.

优选地,所述混合浊液中的钼原子的摩尔浓度为0.1-1.0mol/L。在优选 的实施例中,所述混合浊液中的钼原子的摩尔浓度为0.3-1mol/L。Preferably, the molar concentration of molybdenum atoms in the mixed turbid solution is 0.1-1.0 mol/L. In a preferred embodiment, the molar concentration of molybdenum atoms in the mixed turbid solution is 0.3-1 mol/L.

优选地,所述锰原子与钼原子的摩尔比为0.01-0.5∶1。Preferably, the molar ratio of the manganese atoms to the molybdenum atoms is 0.01-0.5:1.

优选地,所述苯胺与钼原子的摩尔比为2.4-10∶1。Preferably, the molar ratio of aniline to molybdenum atoms is 2.4-10:1.

优选地,所述钼源选自七钼酸铵((NH4)6Mo7O24·4H2O)、钼酸钠和钼 酸钾中的至少一种。Preferably, the molybdenum source is selected from at least one of ammonium heptamolybdate ((NH 4 ) 6 Mo 7 O 24 ·4H 2 O), sodium molybdate and potassium molybdate.

优选地,所述锰盐选自醋酸锰、硝酸锰和氯化锰中的至少一种。Preferably, the manganese salt is selected from at least one of manganese acetate, manganese nitrate and manganese chloride.

优选地,在所述步骤S2中,滴加无机酸调节pH至出现黄色沉淀, 40-80℃下反应2-12小时,经抽滤、洗涤、干燥,得到锰改性的钼胺前驱体。 在优选的实施例中,反应物在水浴锅中进行反应,抽滤产物用乙醇进行充分 洗涤。在一个优选的实施例中,60℃下搅拌反应4小时。Preferably, in the step S2, the pH is adjusted dropwise with an inorganic acid until a yellow precipitate appears, the reaction is carried out at 40-80° C. for 2-12 hours, and the manganese-modified molybdenum amine precursor is obtained by suction filtration, washing and drying. In a preferred embodiment, the reactants are reacted in a water bath, and the suction-filtered product is fully washed with ethanol. In a preferred embodiment, the reaction is stirred at 60°C for 4 hours.

优选地,所述无机酸为选自稀盐酸、稀硫酸和稀硝酸中的至少一种。 在优选的实施例中,无机酸为浓度为0.1-3M的稀盐酸、稀硫酸、或稀硝酸等。 在一个优选的实施例中,所述无机酸为1M HCl溶液。Preferably, the inorganic acid is at least one selected from dilute hydrochloric acid, dilute sulfuric acid and dilute nitric acid. In a preferred embodiment, the inorganic acid is dilute hydrochloric acid, dilute sulfuric acid, or dilute nitric acid with a concentration of 0.1-3M. In a preferred embodiment, the inorganic acid is a 1M HCl solution.

优选地,通过加入无机酸调控混合浊液的pH至4-5。Preferably, the pH of the mixed turbid solution is adjusted to 4-5 by adding inorganic acid.

优选地,在所述步骤S3中,在管式炉中进行煅烧,将煅烧后的产物酸 泡、离心水洗至中性后干燥,得到锰氮共掺杂碳化钼纳米棒。Preferably, in the step S3, calcination is carried out in a tube furnace, and the calcined product is acid-bubble, centrifugally washed to neutrality and then dried to obtain manganese-nitrogen co-doped molybdenum carbide nanorods.

优选地,所述酸泡所使用的酸选自盐酸和硫酸中的至少一种。在一个 优选的实施例中,所述酸泡所使用的酸为0.5M的H2SO4溶液。Preferably, the acid used in the acid foam is selected from at least one of hydrochloric acid and sulfuric acid. In a preferred embodiment, the acid used in the acid bubble is a 0.5M H 2 SO 4 solution.

优选地,在所述步骤S3中,以2-10℃/min的升温速率升至600-800℃ 的煅烧温度下煅烧2-10小时。在优选的实施例中,该煅烧温度为650-750℃。 在一个优选的实施例中,所述煅烧温度为700℃。Preferably, in the step S3, calcination is carried out at a calcination temperature of 600-800° C. for 2-10 hours at a heating rate of 2-10° C./min. In a preferred embodiment, the calcination temperature is 650-750°C. In a preferred embodiment, the calcination temperature is 700°C.

优选地,所述煅烧气氛为惰性气体和氢气的混合气体。在优选的实施 例中,所述煅烧气氛中的氢气的体积含量为0.05-0.25。在优选的实施例中, 所述煅烧气氛为H2和Ar的混合气氛。Preferably, the calcining atmosphere is a mixed gas of inert gas and hydrogen. In a preferred embodiment, the volume content of hydrogen in the calcining atmosphere is 0.05-0.25. In a preferred embodiment, the calcination atmosphere is a mixed atmosphere of H 2 and Ar.

本发明还提供由上述的制备方法得到的锰氮共掺杂碳化钼纳米棒。The present invention also provides the manganese-nitrogen co-doped molybdenum carbide nanorods obtained by the above preparation method.

优选地,所述锰氮共掺杂碳化钼纳米棒由颗粒尺寸均匀的碳化钼纳米 颗粒堆积而成。特别地,所述锰氮共掺杂碳化钼纳米棒具有丰富的孔结构, 有利于电解质的渗入和氢气的溢出。Preferably, the manganese-nitrogen co-doped molybdenum carbide nanorods are formed by stacking molybdenum carbide nanoparticles with uniform particle size. In particular, the manganese-nitrogen co-doped molybdenum carbide nanorods have abundant pore structures, which are favorable for the infiltration of electrolyte and the escape of hydrogen.

本发明还提供上述锰氮共掺杂碳化钼纳米棒作为电催化剂的应用。The present invention also provides the application of the above manganese-nitrogen co-doped molybdenum carbide nanorod as an electrocatalyst.

优选地,所述锰氮共掺杂碳化钼纳米棒用于电解水制氢。Preferably, the manganese-nitrogen co-doped molybdenum carbide nanorods are used for electrolysis of water to produce hydrogen.

优选地,所述锰氮共掺杂碳化钼纳米棒用作酸性介质下的电解水析氢 催化剂。在优选的实施例中,在0.5M H2SO4溶液中,在20mA/cm2电流密度 下的过电位为192-226mV(相对可逆氢电极),塔菲尔斜率为66-103mV/dec, 并且连续运行24h仍保持良好的稳定性。Preferably, the manganese-nitrogen co-doped molybdenum carbide nanorods are used as a catalyst for electrolysis of water for hydrogen evolution in an acidic medium. In a preferred embodiment, in 0.5MH 2 SO 4 solution, the overpotential at 20 mA/cm 2 current density is 192-226 mV (relative to the reversible hydrogen electrode), the Tafel slope is 66-103 mV/dec, and Continuous operation for 24h still maintains good stability.

根据本发明的锰氮共掺杂碳化钼纳米棒的制备方法,流程简单、产量 高、成本低、且易于大规模生产。具体地,本发明利用有机-无机杂化的方法 获得锰改性的钼胺前驱体,然后在还原气氛中煅烧得到锰氮共掺杂碳化钼纳 米棒,这种通过前驱体的制备方法可有效减少团聚。而且,本发明的锰氮共 掺杂碳化钼纳米棒通过掺杂价电子(d5)丰富且电负性小的锰元素来调控碳化 钼的电子结构,加速碳化钼析氢动力学,提高电解水析氢活性。另外,根据 拉曼光谱中探测不到碳典型的D峰和G峰可知,本发明提供的锰氮共掺杂碳 化钼纳米棒不存在表面覆盖污染碳的问题,催化位点可充分暴露出来,从而 得到不含贵金属的高活性电解水析氢催化剂,在酸性介质中表现出良好的电 解水析氢活性和稳定性。According to the preparation method of the manganese-nitrogen co-doped molybdenum carbide nanorods of the present invention, the process is simple, the yield is high, the cost is low, and the mass production is easy. Specifically, the present invention utilizes an organic-inorganic hybridization method to obtain a manganese-modified molybdenum amine precursor, and then calcinations in a reducing atmosphere to obtain manganese-nitrogen co-doped molybdenum carbide nanorods. This preparation method through the precursor can effectively Reduce agglomeration. Moreover, the manganese-nitrogen co-doped molybdenum carbide nanorods of the present invention regulate the electronic structure of molybdenum carbide by doping manganese elements with abundant valence electrons (d 5 ) and low electronegativity, accelerate the hydrogen evolution kinetics of molybdenum carbide, and improve the electrolysis of water. Hydrogen evolution activity. In addition, according to the fact that the typical D peaks and G peaks of carbon are not detected in the Raman spectrum, it can be seen that the manganese-nitrogen co-doped molybdenum carbide nanorods provided by the present invention do not have the problem that the surface is covered with contaminated carbon, and the catalytic sites can be fully exposed. Thereby, a highly active electrolytic water hydrogen evolution catalyst free of precious metals is obtained, which exhibits good electrolytic water hydrogen evolution activity and stability in an acidic medium.

附图说明Description of drawings

图1是不同锰钼配比制备的锰氮共掺杂碳化钼纳米棒的XRD图;Fig. 1 is the XRD pattern of manganese-nitrogen co-doped molybdenum carbide nanorods prepared with different manganese-molybdenum ratios;

图2是样品A和样品B的XRD图;Fig. 2 is the XRD pattern of sample A and sample B;

图3是实施例1制备的锰氮共掺杂碳化钼纳米棒的SEM图(a)和高 倍TEM图(b);Fig. 3 is the SEM image (a) and high magnification TEM image (b) of the manganese-nitrogen co-doped molybdenum carbide nanorods prepared in Example 1;

图4是不同锰钼配比制备的锰氮共掺杂碳化钼纳米棒的拉曼表征;Fig. 4 is the Raman characterization of manganese-nitrogen co-doped molybdenum carbide nanorods prepared with different manganese-molybdenum ratios;

图5是实施例1制备的锰氮共掺杂碳化钼纳米棒的XPS全谱表征;5 is the XPS full spectrum characterization of the manganese-nitrogen co-doped molybdenum carbide nanorods prepared in Example 1;

图6是不同锰钼配比制备的锰氮共掺杂碳化钼纳米棒的电解水制氢催 化性能表征;Fig. 6 is the electrolytic water hydrogen production catalytic performance characterization of manganese-nitrogen co-doped molybdenum carbide nanorods prepared with different manganese-molybdenum ratios;

图7是实施例1制备的锰氮共掺杂碳化钼纳米棒的电解水制氢的稳定 性表征。Fig. 7 is the stability characterization of the electrolysis of water for hydrogen production of the manganese-nitrogen co-doped molybdenum carbide nanorods prepared in Example 1.

具体实施方式Detailed ways

下面结合附图,给出本发明的较佳实施例,并予以详细描述。Below in conjunction with the accompanying drawings, preferred embodiments of the present invention are given and described in detail.

实施例1Example 1

称取碳源苯胺1.25g,七钼酸铵((NH4)6Mo7O24·4H2O)1g,以及醋酸 锰(Mn(C2H3O2)2·4H2O)13.8mg(钼原子的摩尔浓度为0.3mol/L,苯胺与钼 原子的摩尔比为2.4∶1,Mn∶Mo摩尔比为0.01)于烧杯中,加水20mL,超 声分散,加入1M HCl溶液调节pH至4-5,在60℃水浴中搅拌4h后,将黄 色产物抽滤分离,干燥。将干燥后的产物在10%H2/Ar气氛下煅烧到700℃, 保温3h,然后将煅烧后的产物用0.5M的H2SO4溶液泡24h,除去催化剂中 的不稳定物种,最后离心水洗至中性后,干燥即可,所得的产物记为Mn, N-Mo2C-0.01。Weigh out 1.25 g of carbon source aniline, 1 g of ammonium heptamolybdate ((NH 4 ) 6 Mo 7 O 24 ·4H 2 O), and 13.8 mg of manganese acetate (Mn(C 2 H 3 O 2 ) 2 ·4H 2 O) (The molar concentration of molybdenum atoms is 0.3mol/L, the molar ratio of aniline and molybdenum atoms is 2.4:1, and the molar ratio of Mn:Mo is 0.01) in a beaker, add 20 mL of water, ultrasonically disperse, and add 1M HCl solution to adjust pH to 4 -5. After stirring in a 60°C water bath for 4 hours, the yellow product was separated by suction filtration and dried. The dried product was calcined to 700°C in a 10% H 2 /Ar atmosphere, kept for 3 h, and then the calcined product was soaked in 0.5 M H 2 SO 4 solution for 24 h to remove unstable species in the catalyst, and finally centrifuged After washing with water until it becomes neutral, it can be dried, and the obtained product is recorded as Mn, N-Mo 2 C-0.01.

锰氮共掺杂碳化钼纳米棒电解水制氢的电化学测试按以下步骤进行:The electrochemical test of manganese-nitrogen co-doped molybdenum carbide nanorods for electrolysis of water for hydrogen production is carried out according to the following steps:

首先,称取4mg上述产物和0.5mg炭黑分散在2ml异丙醇和 60uLNafion溶液(5%)的混合溶液中,超声得到均匀分散的悬浮液,然后取 80uL上述悬浮液滴到直径为6mm的波碳电极上,自然干燥后即可得到工作 电极;然后电解水制氢性能测试在电化学工作站(CHI760E,上海辰华)进行, 采用三电极体系,以0.5M H2SO4溶液为电解液,石墨棒为对电极,3M KCl 溶液填充的Ag/AgCl电极为参比电极,线性扫描伏安曲线的扫速为5mV/s, 实验数据未进行IR校正,电极电势相对于可逆氢电极(RHE),换算方法如 下:ERHE=EAg/AgCl+0.059*pH+0.209。First, 4 mg of the above product and 0.5 mg of carbon black were weighed and dispersed in a mixed solution of 2 ml of isopropanol and 60 uLNafion solution (5%), sonicated to obtain a uniformly dispersed suspension, and then 80 uL of the above suspension was dropped onto a wave with a diameter of 6 mm. On the carbon electrode, the working electrode can be obtained after natural drying; then the hydrogen production performance test of electrolyzed water is carried out in an electrochemical workstation (CHI760E, Shanghai Chenhua), using a three-electrode system, with 0.5MH 2 SO 4 solution as electrolyte, graphite The rod is the counter electrode, the Ag/AgCl electrode filled with 3M KCl solution is the reference electrode, the scan rate of the linear sweep voltammetry curve is 5mV/s, the experimental data is not IR corrected, and the electrode potential is relative to the reversible hydrogen electrode (RHE), The conversion method is as follows: E RHE =E Ag/AgCl +0.059*pH+0.209.

实施例2Example 2

实施例2中的制备过程和步骤与上述实施例1基本相同,不同的是: 称取乙酸锰(Mn(C2H3O2)2·4H2O)的质量为1.4mg(Mn:Mo摩尔比为0.001), 制得的催化剂记为Mn,N-Mo2C-0.001。催化剂的电解水制氢催化性能表征同The preparation process and steps in Example 2 are basically the same as those in Example 1 above, except that the mass of manganese acetate (Mn(C 2 H 3 O 2 ) 2 ·4H 2 O) was weighed to be 1.4 mg (Mn: Mo The molar ratio is 0.001), and the prepared catalyst is denoted as Mn, N-Mo 2 C-0.001. The catalytic performance of the catalyst for electrolysis of water for hydrogen production is the same as

实施例1。Example 1.

实施例3Example 3

实施例3中的制备过程和步骤与上述实施例1基本相同,不同的是: 称取乙酸锰(Mn(C2H3O2)2·4H2O)的质量为7.0mg(Mn∶Mo摩尔比为0.005), 制得的催化剂记为Mn,N-Mo2C-0.005。催化剂的电解水制氢催化性能表征同The preparation process and steps in Example 3 are basically the same as those in Example 1 above, except that the mass of manganese acetate (Mn(C 2 H 3 O 2 ) 2 ·4H 2 O) was weighed to be 7.0 mg (Mn:Mo The molar ratio is 0.005), and the prepared catalyst is denoted as Mn, N-Mo 2 C-0.005. The catalytic performance of the catalyst for electrolysis of water for hydrogen production is the same as

实施例1。Example 1.

实施例4Example 4

实施例4中的制备过程和步骤与上述实施例1基本相同,不同的是: 称取乙酸锰(Mn(C2H3O2)2·4H2O)的质量为69.4mg(Mn∶Mo摩尔比为0.05), 制得的催化剂记为Mn,N-Mo2C-0.05。催化剂的电解水制氢催化性能表征同实 施例1。The preparation process and steps in Example 4 are basically the same as those in Example 1 above, except that the mass of manganese acetate (Mn(C 2 H 3 O 2 ) 2 ·4H 2 O) was weighed to be 69.4 mg (Mn:Mo The molar ratio is 0.05), and the prepared catalyst is denoted as Mn, N-Mo 2 C-0.05. The characterization of the catalytic performance of the catalyst for electrolysis of water for hydrogen production is the same as that in Example 1.

实施例5Example 5

实施例5中的制备过程和步骤与上述实施例1基本相同,不同的是: 没有加入乙酸锰(Mn(C2H3O2)2·4H2O),制得的催化剂记为Mn,N-Mo2C-0。催 化剂的电解水制氢催化性能表征同实施例1。The preparation process and steps in Example 5 are basically the same as those in Example 1 above, except that manganese acetate (Mn(C 2 H 3 O 2 ) 2 ·4H 2 O) was not added, and the prepared catalyst was denoted as Mn, N-Mo 2 C-0. The characterization of the catalytic performance of the catalyst for electrolysis of water for hydrogen production is the same as that in Example 1.

实施例6Example 6

实施例6中的制备过程和步骤与上述实施例1基本相同,不同的是: 苯胺与钼原子的摩尔比为10∶1,钼原子的摩尔浓度为1.0mol/L,Mn∶Mo摩尔 比为0.5。该样品标记为样品A。The preparation process and steps in Example 6 are basically the same as in Example 1 above, except that the molar ratio of aniline and molybdenum atom is 10:1, the molar concentration of molybdenum atom is 1.0mol/L, and the Mn:Mo molar ratio is 0.5. This sample is labeled Sample A.

实施例7Example 7

实施例7中的制备过程和步骤与上述实施例1基本相同,不同的是: 苯胺与钼原子的摩尔比为1:1,钼原子的摩尔浓度为0.3mol/L,Mn∶Mo摩尔 比为0.05。该样品标记为样品B。The preparation process and steps in Example 7 are basically the same as those in Example 1 above, except that the molar ratio of aniline and molybdenum atom is 1:1, the molar concentration of molybdenum atom is 0.3mol/L, and the Mn:Mo molar ratio is 0.05. This sample is labeled sample B.

下表1为不同锰钼配比制备的锰氮共掺杂碳化钼纳米棒的锰含量的 ICP-OES结果,表明锰成功掺入到碳化钼晶体中。Table 1 below is the ICP-OES result of the manganese content of manganese-nitrogen co-doped molybdenum carbide nanorods prepared with different manganese-molybdenum ratios, indicating that manganese is successfully incorporated into the molybdenum carbide crystal.

表1Table 1

Figure BDA0002115802530000061
Figure BDA0002115802530000061

图1为不同锰钼配比制备的锰氮共掺杂碳化钼纳米棒的XRD图,从图 1中可以看出,制备的催化剂为β-Mo2C,且一定含量范围的锰掺杂不会对晶 体成分有影响。Figure 1 shows the XRD patterns of manganese-nitrogen co-doped molybdenum carbide nanorods prepared with different ratios of manganese and molybdenum. It can be seen from Figure 1 that the prepared catalyst is β-Mo 2 C, and the manganese doping in a certain content range does not will affect the crystal composition.

图2为样品A和样品B的XRD图。从图2中可以看出,样品A和样 品B均为β-Mo2C。Figure 2 is the XRD pattern of sample A and sample B. It can be seen from Figure 2 that both sample A and sample B are β-Mo 2 C.

图3为实施例1制备的锰氮共掺杂碳化钼纳米棒的SEM图(a)和高 倍TEM图(b),这种碳化钼纳米棒由颗粒尺寸均匀的碳化钼纳米颗粒堆积而 成,具有丰富的孔结构,且高倍透射电镜下没有碳的晶格条纹。Fig. 3 is the SEM image (a) and the high magnification TEM image (b) of the manganese-nitrogen co-doped molybdenum carbide nanorods prepared in Example 1. The molybdenum carbide nanorods are formed by stacking molybdenum carbide nanoparticles with uniform particle size. It has abundant pore structure and no carbon lattice fringes under high magnification transmission electron microscope.

图4为不同锰钼配比制备的锰氮共掺杂碳化钼纳米棒的拉曼表征,拉 曼图谱中只有碳化钼的特征峰,不含碳的特征峰(D峰、G峰),表明制备的 催化剂表面没有被污染碳覆盖。Figure 4 shows the Raman characterization of manganese-nitrogen co-doped molybdenum carbide nanorods prepared with different ratios of manganese and molybdenum. In the Raman spectrum, there are only characteristic peaks of molybdenum carbide and no characteristic peaks of carbon (peak D and peak G), indicating that The prepared catalyst surface was not covered with contaminating carbon.

图5为实施例1制备的锰氮共掺杂碳化钼纳米棒的XPS全谱表征,全 谱中的氮信号表明氮元素掺入碳化钼晶体中。Figure 5 is the XPS full spectrum characterization of the manganese-nitrogen co-doped molybdenum carbide nanorods prepared in Example 1, and the nitrogen signal in the full spectrum indicates that nitrogen is incorporated into the molybdenum carbide crystal.

图6为不同锰钼配比制备的锰氮共掺杂碳化钼纳米棒的电解水制氢催 化性能表征,(a)为线性扫描伏安曲线,(b)为塔菲尔曲线。从(a)中可以 看出,当电流密度为20mA/cm2,Mn、N-Mo2C-0、Mn、N-Mo2C-0.001、Mn、 N-Mo2C-0.005、Mn、N-Mo2C-0.01、Mn、N-Mo2C-0.05所需要的过电位分别 为226mV、208mV、195mV、192mV、218mV,这表明Mn、N-Mo2C-0.01 的电解水制氢的催化性能最好。从(b)中可以看出,Mn、N-Mo2C-0、Mn、 N-Mo2C-0.001、Mn、N-Mo2C-0.005、Mn、N-Mo2C-0.01、Mn、N-Mo2C-0.05 的塔菲尔斜率分别为103mV/dec、72mV/dec、70mV/dec、66mV/dec、88mV/dec, 表明它们的速率限制步骤都是Volmer-Heyrovsky步骤,其中,Volmer-Heyrovsky步骤是电解水制氢过程中,氢质子的吸附-脱附步骤,根据 塔菲尔斜率可以得到反应的速率限制步骤,塔菲尔斜率越小越好。Figure 6 shows the characterization of the catalytic performance of the manganese-nitrogen co-doped molybdenum carbide nanorods prepared with different ratios of manganese and molybdenum for the electrolysis of water for hydrogen production, (a) is the linear sweep voltammetry curve, (b) is the Tafel curve. It can be seen from (a) that when the current density is 20 mA/cm 2 , Mn, N-Mo 2 C-0, Mn, N-Mo 2 C-0.001, Mn, N-Mo 2 C-0.005, Mn, The overpotentials required for N-Mo 2 C-0.01, Mn, and N-Mo 2 C-0.05 were 226mV, 208mV, 195mV, 192mV, and 218mV, respectively, which indicated that the electrolysis of Mn and N-Mo 2 C-0.01 could produce hydrogen by electrolysis of water. the best catalytic performance. As can be seen from (b), Mn, N-Mo2C - 0, Mn, N-Mo2C - 0.001, Mn, N-Mo2C - 0.005, Mn, N-Mo2C - 0.01, Mn , the Tafel slopes of N-Mo 2 C-0.05 are 103mV/dec, 72mV/dec, 70mV/dec, 66mV/dec, 88mV/dec, respectively, indicating that their rate limiting steps are Volmer-Heyrovsky steps, where, The Volmer-Heyrovsky step is the adsorption-desorption step of hydrogen protons in the process of electrolysis of water for hydrogen production. According to the Tafel slope, the rate-limiting step of the reaction can be obtained. The smaller the Tafel slope, the better.

图7为实施例1制备的锰氮共掺杂碳化钼纳米棒的电解水制氢的稳定 性表征(i-t曲线),在运行24h后,电流密度仍然保持在7.2mA/cm2左右,表 明其良好的稳定性。Figure 7 shows the stability characterization (it curve) of the electrolysis of water for hydrogen production of the manganese-nitrogen co-doped molybdenum carbide nanorods prepared in Example 1. After running for 24 h, the current density still remains at about 7.2 mA/cm 2 , indicating that its good stability.

以上所述的,仅为本发明的较佳实施例,并非用以限定本发明的范围, 本发明的上述实施例还可以做出各种变化。即凡是依据本发明申请的权利要 求书及说明书内容所作的简单、等效变化与修饰,皆落入本发明专利的权利 要求保护范围。本发明未详尽描述的均为常规技术内容。The above descriptions are only preferred embodiments of the present invention, and are not intended to limit the scope of the present invention. Various changes can also be made to the above-mentioned embodiments of the present invention. That is, all simple, equivalent changes and modifications made according to the claims and description content of the application for the present invention all fall into the scope of protection of the claims of the present invention. What is not described in detail in the present invention is conventional technical content.

Claims (10)

1. The preparation method of the manganese-nitrogen co-doped molybdenum carbide nanorod is characterized by comprising the following steps of:
s1, adding a molybdenum source, manganese salt and aniline into water, and performing ultrasonic treatment to form a mixed turbid liquid, wherein the molar ratio of manganese atoms to molybdenum atoms is 0.001-0.5:1, and the molar ratio of aniline to molybdenum atoms is 1-10: 1;
s2, regulating the pH value of the mixed turbid liquid to 3-6 by adding inorganic acid, and reacting to obtain a manganese-modified molybdenum amine precursor;
and S3, calcining the manganese modified molybdenum amine precursor in a reductive calcining atmosphere to obtain the manganese-nitrogen co-doped molybdenum carbide nanorod without carbon on the surface.
2. The method according to claim 1, wherein the molar concentration of molybdenum atoms in the mixed turbid liquid is 0.1-1.0 mol/L.
3. The method according to claim 1, wherein the molybdenum source is at least one selected from ammonium heptamolybdate, sodium molybdate, and potassium molybdate.
4. The method according to claim 1, wherein the manganese salt is at least one selected from the group consisting of manganese acetate, manganese nitrate and manganese chloride.
5. The production method according to claim 1, wherein the inorganic acid is at least one selected from the group consisting of dilute hydrochloric acid, dilute sulfuric acid, and dilute nitric acid.
6. The method as claimed in claim 1, wherein in step S3, the calcination is carried out at a calcination temperature raised to 600-800 ℃ at a temperature raising rate of 2-10 ℃/min for 2-10 hours.
7. The method according to claim 1, wherein the calcining atmosphere is a mixed gas of an inert gas and hydrogen gas.
8. The method according to claim 7, wherein the hydrogen gas is contained in the calcination atmosphere in an amount of 0.05 to 0.25 by volume.
9. Manganese-nitrogen-codoped molybdenum carbide nanorod obtained according to the preparation method of any one of claims 1-8.
10. Use of the manganese-nitrogen co-doped molybdenum carbide nanorod according to claim 9 as an electrocatalyst.
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