CN114921805B - MoO2-Mo2C-C电催化析氢催化剂及制备方法 - Google Patents

MoO2-Mo2C-C电催化析氢催化剂及制备方法 Download PDF

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CN114921805B
CN114921805B CN202210540519.3A CN202210540519A CN114921805B CN 114921805 B CN114921805 B CN 114921805B CN 202210540519 A CN202210540519 A CN 202210540519A CN 114921805 B CN114921805 B CN 114921805B
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唐辉
张兴龙
廖天浩
朱斌
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Abstract

一种MoO2‑Mo2C‑C电催化析氢催化剂及制备方法,属于催化剂制备技术领域。所述催化剂包括MoO2颗粒,包覆于MoO2颗粒表面的Mo2C层,以及包覆于Mo2C层表面的碳层;MoO2颗粒与Mo2C层形成异质结构,MoO2颗粒的粒径为20~500nm,Mo2C层的厚度为5~20nm;碳层为多孔结构,孔径为1~5nm,厚度为20~100nm。本发明采用等离子体增强化学气相沉积法一步制得了MoO2‑Mo2C‑C催化剂,制得的催化剂具有核壳结构和较高的比表面积,可应用于电催化析氢,具有良好的全pH电催化析氢活性,在清洁能源生产和环境保护方面具有重要的实际应用价值。

Description

MoO2-Mo2C-C电催化析氢催化剂及制备方法
技术领域
本发明属于催化剂制备技术领域,具体涉及一种核壳多孔结构MoO2-Mo2C-C电催化析氢催化剂及制备方法。
背景技术
随着世界经济的快速发展,人类社会对化石燃料的消耗不断增加,由此带来的气候变化和环境污染问题亟待解决。在各国推动能源转型的大背景下,清洁和可再生能源的利用迫在眉睫。氢能具有来源广泛、可再生、高燃烧热、零污染等诸多优势,受到了越来越多研究者的广泛关注。目前,制备氢气主要采用电解水的方法,电解水制氢方便高效,产物氢气也易于分离,具有良好的应用前景。但是,由于电解水所需电压大,能耗高,导致制氢成本高,因此开发电催化剂降低电解水的电压以便于商业化应用显得尤为重要。铂基材料由于其独特的贵金属电子结构,具有很好的电催化析氢性能,但由于其成本高昂,并不适合大规模商业化应用,因此开发低成本高活性的电催化析氢催化剂非常必要。
发明内容
本发明的目的在于,针对背景技术存在的缺陷,提出了一种MoO2-Mo2C-C电催化析氢催化剂及制备方法。
为实现上述目的,本发明采用的技术方案如下:
一种MoO2-Mo2C-C电催化析氢催化剂,包括MoO2颗粒,包覆于MoO2颗粒表面的Mo2C层,以及包覆于Mo2C层表面的碳层;其中,所述MoO2颗粒与Mo2C层形成异质结构,所述MoO2颗粒的粒径为20~500nm,Mo2C层的厚度为5~20nm;所述碳层为多孔结构,碳层孔径为1~5nm,厚度为20~100nm。
一种MoO2-Mo2C-C电催化析氢催化剂的制备方法,包括以下步骤:
步骤1、将MoO3置于石英舟,并放入等离子体增强化学气相沉积系统;
步骤2、采用等离子体增强化学气相沉积法在MoO3表面沉积Mo2C层和碳层,得到MoO2-Mo2C-C三层结构;其中,反应气体为甲烷,等离子体放电功率为300W~800W,放电时间为5min~8min,反应压力为5Pa~50Pa,甲烷的流量为50~150mL/min;
步骤3、步骤2得到的MoO2-Mo2C-C三层结构在去离子水和乙醇中清洗,烘干,即可得到所述MoO2-Mo2C-C电催化析氢催化剂。
进一步的,所述MoO3的粒径为20~500nm。
与现有技术相比,本发明的有益效果为:
本发明提供的一种MoO2-Mo2C-C电催化析氢催化剂及制备方法,采用等离子体增强化学气相沉积法一步制得了MoO2-Mo2C-C催化剂,制得的催化剂具有核壳结构和较高的比表面积,可应用于电催化析氢,具有良好的全pH电催化析氢活性,在清洁能源生产和环境保护方面具有重要的实际应用价值。
附图说明
图1为实施例1制备得到的MoO2-Mo2C-C电催化析氢催化剂的SEM图;
图2为实施例3制备得到的MoO2-Mo2C-C电催化析氢催化剂的SEM图;
图3为实施例2制备得到的MoO2-Mo2C-C电催化析氢催化剂的TEM图;
图4为实施例2制备得到的MoO2-Mo2C-C电催化析氢催化剂的HRTEM图;
图5为实施例2制备得到的MoO2-Mo2C-C电催化析氢催化剂的XRD图;
图6为实施例2制备得到的MoO2-Mo2C-C电催化析氢催化剂的XPS全谱;
图7为实施例2制备得到的MoO2-Mo2C-C电催化析氢催化剂在酸性条件下的线性极化曲线;
图8为实施例2制备得到的MoO2-Mo2C-C电催化析氢催化剂在碱性条件下的线性极化曲线;
图9为实施例2制备得到的MoO2-Mo2C-C电催化析氢催化剂在碱性条件下不同扫速下的CV曲线图;
图10为实施例2制备得到的MoO2-Mo2C-C电催化析氢催化剂根据不同扫速下测得的CV图拟合得到的双电层电容图。
具体实施方式
下面结合具体实施例对本发明做进一步解释和说明。
实施例1
一种MoO2-Mo2C-C电催化析氢催化剂的制备方法,包括以下步骤:
步骤1、称取1g粒径为200nm的MoO3置于石英舟,并放入等离子体增强化学气相沉积系统;
步骤2、采用等离子体增强化学气相沉积法在MoO3表面沉积Mo2C层和碳层,得到MoO2-Mo2C-C三层结构;其中,反应气体为甲烷,等离子体放电功率为300W,放电时间为8min,反应压力为5Pa,甲烷的流量为50mL/min;
步骤3、步骤2得到的MoO2-Mo2C-C三层结构在去离子水和乙醇中分别清洗3次,烘干,即可得到所述MoO2-Mo2C-C电催化析氢催化剂,制得的催化剂中Mo2C层的厚度为8nm,碳层厚度为30nm、孔径为2nm。
实施例2
一种MoO2-Mo2C-C电催化析氢催化剂的制备方法,包括以下步骤:
步骤1、称取1g粒径为300nm的MoO3置于石英舟,并放入等离子体增强化学气相沉积系统;
步骤2、采用等离子体增强化学气相沉积法在MoO3表面沉积Mo2C层和碳层,得到MoO2-Mo2C-C三层结构;其中,反应气体为甲烷,等离子体放电功率为400W,放电时间为6min,反应压力为50Pa,甲烷的流量为100mL/min;
步骤3、步骤2得到的MoO2-Mo2C-C三层结构在去离子水和乙醇中分别清洗3次,烘干,即可得到所述MoO2-Mo2C-C电催化析氢催化剂,制得的催化剂中Mo2C层的厚度为10nm,碳层厚度为40nm、孔径为3nm。
实施例3
一种MoO2-Mo2C-C电催化析氢催化剂的制备方法,包括以下步骤:
步骤1、称取1g粒径为500nm的MoO3置于石英舟,并放入等离子体增强化学气相沉积系统;
步骤2、采用等离子体增强化学气相沉积法在MoO3表面沉积Mo2C层和碳层,得到MoO2-Mo2C-C三层结构;其中,反应气体为甲烷,等离子体放电功率为800W,放电时间为5min,反应压力为25Pa,甲烷的流量为150mL/min;
步骤3、步骤2得到的MoO2-Mo2C-C三层结构在去离子水和乙醇中分别清洗3次,烘干,即可得到所述MoO2-Mo2C-C电催化析氢催化剂,制得的催化剂中Mo2C层的厚度为20nm,碳层厚度为80nm、孔径为5nm。
图1为实施例1制备得到的MoO2-Mo2C-C电催化析氢催化剂的SEM图;由图1可知,制得的MoO2-Mo2C-C电催化析氢催化剂为片层结构,片层厚度约为200nm。
图2为实施例3制备得到的MoO2-Mo2C-C电催化析氢催化剂的SEM图;由图2可知,制得的MoO2-Mo2C-C电催化析氢催化剂为片层结构,片层厚度约为500nm。
图3为实施例2制备得到的MoO2-Mo2C-C电催化析氢催化剂的低倍率TEM图;由图3可知,制得的MoO2-Mo2C-C电催化析氢催化剂为核壳多孔结构,Mo2C层的厚度为10nm,碳层为多孔结构,其厚度为40nm、孔径为3nm。多孔碳层结构有利于水和氢离子的扩散,增大了水和氢离子与电催化剂的接触面积,有效提高了MoO2-Mo2C-C的电催化活性。
图4为实施例2制备得到的MoO2-Mo2C-C电催化析氢催化剂的HRTEM图;由图4可知,制得的MoO2-Mo2C-C电催化析氢催化剂为三层核壳结构,在图中可以观察到MoO2的晶格结构和Mo2C的晶格结构,其中内层晶格间距有两处d=0.243nm和d=0.342nm,分别归属于MoO2的(-211)晶面和(011)晶面,中间层晶格间距有两处,d=0.229nm和d=0.261nm,分别归属于Mo2C的(101)晶面和(100)晶面。Mo2C层约为10nm,MoO2与Mo2C层形成MoO2-Mo2C异质结构,异质结构的形成可以有效提高MoO2-Mo2C-C的电催化活性。
图5为实施例2制备得到的MoO2-Mo2C-C电催化析氢催化剂的XRD图;由图5可知,实施例2制备得到的MoO2-Mo2C-C电催化析氢催化剂,有明显的MoO2和Mo2C的特征衍射峰,表明成功制得了MoO2-Mo2C-C三层核壳结构。
图6为实施例2制备得到的MoO2-Mo2C-C电催化析氢催化剂的XPS全谱;由图6可知,MoO2-Mo2C-C主要由C、Mo、O三种元素组成。
图7为实施例2制备得到的MoO2-Mo2C-C电催化析氢催化剂在酸性条件下的线性极化曲线;由图7可知,实施例2制备得到的MoO2-Mo2C-C电催化析氢催化剂的过电位(电流密度为10mA/cm2的电位)为170mV。
图8为实施例2制备得到的MoO2-Mo2C-C电催化析氢催化剂在碱性条件下的线性极化曲线;由图8可知,实施例2制备得到的MoO2-Mo2C-C电催化析氢催化剂的过电位(电流密度为10mA/cm2的电位)为130mV。
图9为实施例2制备得到的MoO2-Mo2C-C电催化析氢催化剂在碱性条件下不同扫速下的CV曲线;由图9可知,实施例2制备得到的MoO2-Mo2C-C电催化析氢催化剂CV曲线包围面积较大,表明有着较大的电化学活性表面积。
图10为实施例2制备得到的MoO2-Mo2C-C电催化析氢催化剂在碱性条件下根据不同扫速曲线下的CV曲线图拟合得到的双电层电容图;由图10可知,实施例2制备得到的MoO2-Mo2C-C电催化析氢催化剂的双电层电容Cdl=50.7mF/cm2,电化学活性表面积为ECSA=Cdl/(40uF/cm-4)=1.27×103cm2

Claims (3)

1.一种MoO2-Mo2C-C电催化析氢催化剂,其特征在于,包括MoO2颗粒,包覆于MoO2颗粒表面的Mo2C层,以及包覆于Mo2C层表面的碳层;其中,所述MoO2颗粒与Mo2C层形成异质结构,所述MoO2颗粒的粒径为20~500nm,Mo2C层的厚度为5~20nm;所述碳层为多孔结构,碳层孔径为1~5nm,厚度为20~100nm。
2.一种如权利要求1所述MoO2-Mo2C-C电催化析氢催化剂的制备方法,其特征在于,包括以下步骤:
步骤1、将MoO3置于石英舟,并放入等离子体增强化学气相沉积系统;
步骤2、采用等离子体增强化学气相沉积法在MoO3表面沉积Mo2C层和碳层,得到MoO2-Mo2C-C三层结构;其中,反应气体为甲烷,等离子体放电功率为300W~800W,放电时间为5min~8min,反应压力为5Pa~50Pa,甲烷的流量为50~150mL/min;
步骤3、步骤2得到的MoO2-Mo2C-C三层结构在去离子水和乙醇中清洗,烘干,即可得到所述MoO2-Mo2C-C电催化析氢催化剂。
3.根据权利要求2所述的MoO2-Mo2C-C电催化析氢催化剂的制备方法,其特征在于,所述MoO3的粒径为20~500nm。
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