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CN111408366A - A kind of preparation method of carbon-supported metal nanocluster catalyst - Google Patents

A kind of preparation method of carbon-supported metal nanocluster catalyst Download PDF

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CN111408366A
CN111408366A CN202010139848.8A CN202010139848A CN111408366A CN 111408366 A CN111408366 A CN 111408366A CN 202010139848 A CN202010139848 A CN 202010139848A CN 111408366 A CN111408366 A CN 111408366A
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CN111408366B (en
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张显
吴守良
刘俊
张海民
梁长浩
王新磊
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Hefei Gushui New Energy Technology Co ltd
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/38Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/40Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
    • B01J23/42Platinum
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/30Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
    • B01J35/391Physical properties of the active metal ingredient
    • B01J35/393Metal or metal oxide crystallite size
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/30Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
    • B01J35/391Physical properties of the active metal ingredient
    • B01J35/394Metal dispersion value, e.g. percentage or fraction
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    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
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    • Y02E60/30Hydrogen technology
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Abstract

The invention discloses a preparation method of a carbon-loaded metal nanocluster catalyst, which relates to the field of preparation of metal nanocluster catalysts and comprises the following preparation steps: 1) soaking the carbon carrier into an acid treatment solution, and then filtering and washing to prepare carbon carrier powder rich in functional groups; 2) soaking the carbon carrier powder rich in functional groups into a soluble metal salt solution, and carrying out washing and freeze drying after adsorption to prepare a metal adsorption carbon carrier material; 3) putting the metal-adsorbed carbon carrier material into volatile mercaptan vapor for fumigation treatment to prepare a mercaptan-metal-carbon carrier composite material; 4) calcining the mercaptan-metal-carbon carrier composite material in a protective atmosphere to prepare the carbon-supported metal nanocluster catalyst; according to the invention, metal ions are adsorbed on the carbon material after acid treatment, and then the metal nanocluster catalyst with the sulfur fixed on the surface is prepared by adopting a mercaptan fumigation method, wherein the metal nanoclusters of the catalyst are small in size and good in dispersity.

Description

一种碳负载金属纳米团簇催化剂的制备方法A kind of preparation method of carbon-supported metal nanocluster catalyst

技术领域technical field

本发明涉及金属团簇催化剂制备领域,尤其涉及一种碳负载金属纳米团簇催化剂的制备方法。The invention relates to the field of metal cluster catalyst preparation, in particular to a preparation method of a carbon-supported metal nano-cluster catalyst.

背景技术Background technique

金属团簇催化剂借其独特的表面效应、体积效应和量子尺寸效应,展现了纳米催化材料优异的催化性能,广泛应用于化工领域中的低温催化一氧化碳(CO)氧化、燃料电池反应、低温水煤气转换反应和氮氧化物(NOx)催化分解等,被称为第四代催化剂。金属团簇催化剂的尺寸形貌、原子组成、表面环境以及载体都对催化剂的催化性能有着重要的影响。Metal cluster catalysts exhibit excellent catalytic performance of nano-catalyst materials by virtue of their unique surface effects, volume effects and quantum size effects, and are widely used in low-temperature catalytic carbon monoxide (CO) oxidation, fuel cell reactions, and low-temperature water-gas conversion in the chemical industry. Reactions and catalytic decomposition of nitrogen oxides (NOx), etc., are called fourth-generation catalysts. The size, morphology, atomic composition, surface environment and support of metal cluster catalysts have important effects on the catalytic performance of the catalysts.

目前大部分的金属纳米催化剂都是通过溶液相合成的,为了防止其在应用过程中团聚,还需将其负载到载体上。然而在溶液相合成的金属纳米团簇催化剂表面会存在大量表面活性剂,对其在催化性能的提升造成严重的阻碍,然而直接去除团簇表面的表面活性剂又会造成金属纳米团簇催化剂团聚,使其催化性能下降。At present, most of the metal nanocatalysts are synthesized by solution phase, in order to prevent their agglomeration during the application process, they also need to be supported on a carrier. However, there will be a large amount of surfactant on the surface of the metal nanocluster catalyst synthesized in solution phase, which will seriously hinder the improvement of its catalytic performance. However, the direct removal of the surfactant on the surface of the cluster will cause the metal nanocluster catalyst to agglomerate. , resulting in a decrease in catalytic performance.

例如,一种在中国专利文献上公开“一种金属团簇光稳定性催化剂的制备方法及其应用”,其公告号CN109499567A,其公开了一种金属团簇光稳定性催化剂的制备方法及,通过表面性质调控和/或界面修饰法组合策略提高金属团簇的光稳定性,然而该催化剂通过溶液相合成,表面会存在大量表面活性剂,对其在催化性能的提升造成了严重的阻碍。For example, a Chinese patent document discloses "a preparation method of a metal cluster photostability catalyst and its application", its bulletin number CN109499567A, which discloses a preparation method of a metal cluster photostability catalyst and, The photostability of metal clusters can be improved by a combination strategy of surface property control and/or interface modification. However, the catalyst is synthesized in solution phase, and there are a large number of surfactants on the surface, which seriously hinders the improvement of its catalytic performance.

发明内容SUMMARY OF THE INVENTION

本发明是为了克服目前溶液相合成的金属纳米团簇催化剂表面会存在大量表面活性剂,对其在催化性能的提升造成严重的阻碍,然而直接去除团簇表面的表面活性剂又会造成金属纳米团簇催化剂团聚,使其催化性能下降等问题,提出了一种碳负载金属纳米团簇催化剂的制备方法。The present invention is to overcome the existence of a large number of surfactants on the surface of the metal nanocluster catalyst currently synthesized in solution phase, which seriously hinders the improvement of its catalytic performance. However, directly removing the surfactant on the surface of the cluster will cause metal nanocluster The cluster catalyst agglomerates, which reduces its catalytic performance. A preparation method of carbon-supported metal nanocluster catalyst is proposed.

为了实现上述目的,本发明采用以下技术方案:In order to achieve the above object, the present invention adopts the following technical solutions:

一种碳负载金属纳米团簇催化剂的制备方法,包括以下制备步骤:A preparation method of a carbon-supported metal nanocluster catalyst, comprising the following preparation steps:

1)将碳载体浸泡至酸处理液中,随后过滤洗涤,制备得到富官能团碳载体粉末;1) Soak the carbon carrier in the acid treatment solution, then filter and wash to prepare the functional group-rich carbon carrier powder;

2)将富官能团碳载体粉末浸泡至可溶性金属盐溶液中,吸附后洗涤、冷冻干燥,制备得到金属吸附碳载体材料;2) soaking the functional group-rich carbon carrier powder in a soluble metal salt solution, washing and freeze-drying after adsorption, to prepare a metal-adsorbing carbon carrier material;

3)将金属吸附碳载体材料置于挥发的硫醇蒸气中进行熏蒸处理,制备得到硫醇-金属-碳载体复合材料;3) The metal-adsorbed carbon carrier material is placed in the volatilized mercaptan vapor for fumigation treatment to prepare a mercaptan-metal-carbon carrier composite material;

4)将硫醇-金属-碳载体复合材料在保护气氛下进行煅烧,制备得到碳负载金属纳米团簇催化剂。4) The thiol-metal-carbon support composite material is calcined under a protective atmosphere to prepare a carbon-supported metal nanocluster catalyst.

本发明首先将碳载体浸泡至酸处理液中进行酸处理,制备得到的富官能团碳载体粉末表面富含吸附基团羟基和羧基,浸泡至可溶性金属盐溶液中后富官能团碳载体粉末利用表面吸附基团吸附金属离子,随后将金属吸附碳载体材料置于挥发的硫醇蒸气中进行熏蒸处理,此时,硫醇分子缓慢挥发扩散,并缓慢得与金属吸附碳载体材料吸附的金属形成金属硫醇配位化合物,防止金属团簇的团聚,制备得到硫醇-金属-碳载体复合材料,最后在保护气氛下进行高温煅烧,将金属硫醇配位化合物原位还原,此时,硫醇分子能够防止高温还原中金属团簇的团聚,同时高温煅烧将硫醇分子烷基碳化,从而获得表面有硫固定的碳负载金属纳米团簇催化剂,此时金属团簇表面键合的硫原子还能够对金属团聚形成保护,防止催化剂在储存与使用过程中被氧化,从而提高催化剂性能的稳定性。In the present invention, the carbon carrier is first soaked in an acid treatment solution for acid treatment, and the surface of the prepared functional group-rich carbon carrier powder is rich in adsorption groups of hydroxyl and carboxyl groups. After soaking in a soluble metal salt solution, the functional group-rich carbon carrier powder utilizes surface adsorption The group adsorbs metal ions, and then the metal-adsorbed carbon support material is placed in the volatilized mercaptan vapor for fumigation. At this time, the thiol molecules slowly volatilize and diffuse, and slowly form metal sulfur with the metal adsorbed by the metal-adsorbed carbon support material. The alcohol coordination compound prevents the agglomeration of metal clusters, and the thiol-metal-carbon support composite material is prepared. Finally, high temperature calcination is carried out in a protective atmosphere to reduce the metal thiol coordination compound in situ. At this time, the thiol molecule It can prevent the agglomeration of metal clusters in high-temperature reduction, and at the same time, high-temperature calcination will carbonize the thiol molecule alkyl groups, so as to obtain carbon-supported metal nanocluster catalysts with sulfur fixed on the surface. At this time, the sulfur atoms bound to the surface of metal clusters can also It forms protection for metal agglomeration and prevents the catalyst from being oxidized during storage and use, thereby improving the stability of catalyst performance.

作为优选,步骤1)所述碳载体包括活性炭、导电炭黑、碳纸、碳布、石墨烯中一种或多种。Preferably, the carbon carrier in step 1) includes one or more of activated carbon, conductive carbon black, carbon paper, carbon cloth, and graphene.

碳载体为石墨化的碳材料。The carbon support is a graphitized carbon material.

作为优选,步骤1)所述酸处理液包括食人鱼溶液;所述碳载体和酸处理液的质量比为0.5-3.5:100;所述浸泡时间为10-48h;所述过滤洗涤时,用去离子水洗涤至最后的滤出液体的pH为6-7之间。Preferably, the acid treatment solution in step 1) includes piranha solution; the mass ratio of the carbon carrier and the acid treatment solution is 0.5-3.5:100; the soaking time is 10-48h; during the filtration and washing, use Wash with deionized water until the pH of the final filtrate is between 6-7.

在该比例下,碳载体酸处理的效果更好。Under this ratio, the effect of carbon support acid treatment is better.

作为优选,步骤2)所述可溶性金属盐溶液包括Pt盐、Au盐、Ru盐、Rh盐、Fe盐、Co盐、Ni盐、Pd盐、Ag盐的一种或多种混合溶液;所述可溶性金属盐溶液为0.005-5 mol/L。Preferably, in step 2) the soluble metal salt solution includes one or more mixed solutions of Pt salt, Au salt, Ru salt, Rh salt, Fe salt, Co salt, Ni salt, Pd salt, and Ag salt; the The soluble metal salt solution is 0.005-5 mol/L.

作为优选,步骤2)所述富官能团碳载体粉末与可溶性金属盐溶液的0.1-3.5:100;浸泡时在25-99℃下保温5-20h。Preferably, in step 2), the ratio of the functional group-rich carbon carrier powder to the soluble metal salt solution is 0.1-3.5:100; when soaking, the temperature is kept at 25-99° C. for 5-20 hours.

在该比例条件下,富官能团碳载体粉末吸附效果较好。Under the condition of this ratio, the adsorption effect of the functional group-rich carbon carrier powder is better.

作为优选,步骤3)所述熏蒸处理为在密闭真空环境或惰性气体环境中,10-220 ℃下熏蒸5-100h。Preferably, the fumigation treatment in step 3) is fumigation at 10-220° C. for 5-100 hours in a closed vacuum environment or an inert gas environment.

作为优选,所述步骤3)所述硫醇包括甲硫醇、乙硫醇、辛硫醇、环己硫醇、环戊硫醇、正十二硫醇、2-丙基硫醇、庚硫醇、苯乙硫醇、丁硫醇中的一种或多种。Preferably, in the step 3), the mercaptan includes methyl mercaptan, ethane mercaptan, octane mercaptan, cyclohexane mercaptan, cyclopentane mercaptan, n-dodecane mercaptan, 2-propyl mercaptan, heptyl thiol One or more of alcohol, phenylethanethiol and butanethiol.

作为优选,步骤4)所述煅烧为以5-10℃/min的升温速率升温至300-700℃,保温煅烧1-4h。Preferably, the calcination in step 4) is to raise the temperature to 300-700° C. at a heating rate of 5-10° C./min, and keep calcined for 1-4 hours.

因此,本发明具有如下有益效果:本发明将金属离子吸附于酸处理之后的碳材料上,随后采用硫醇熏蒸的方法,制备得到表面有硫固定的金属纳米团簇催化剂,催化剂的金属纳米团簇尺寸小,分散度好,可有效提高金属的利用率,降低燃料电池中金属的使用量。Therefore, the present invention has the following beneficial effects: the present invention adsorbs metal ions on the carbon material after acid treatment, and then adopts the method of mercaptan fumigation to prepare a metal nanocluster catalyst with fixed sulfur on the surface, and the metal nanocluster of the catalyst is prepared. The cluster size is small and the dispersion is good, which can effectively improve the utilization rate of metals and reduce the usage of metals in fuel cells.

附图说明Description of drawings

图1是本发明实施例1碳负载金属纳米团簇催化剂的TEM图。FIG. 1 is a TEM image of the carbon-supported metal nanocluster catalyst in Example 1 of the present invention.

图2是本发明实施例1碳负载金属纳米团簇催化剂的暗场下STEM图。FIG. 2 is an STEM image of the carbon-supported metal nanocluster catalyst in Example 1 of the present invention under dark field.

图3是本发明实施例1碳负载金属纳米团簇催化剂的XRD图。3 is the XRD pattern of the carbon-supported metal nanocluster catalyst in Example 1 of the present invention.

图4是本发明实施例1碳负载金属纳米团簇催化剂与Johon Matthey 型商业20%Pt/C催化剂在相同测试条件下的ORR催化性能对比图。4 is a graph showing the comparison of the ORR catalytic performance of the carbon-supported metal nanocluster catalyst of Example 1 of the present invention and the Johon Matthey type commercial 20% Pt/C catalyst under the same test conditions.

具体实施方式Detailed ways

下面结合具体实施方式对本发明做进一步的描述。The present invention will be further described below in conjunction with specific embodiments.

实施例1:一种碳负载金属纳米团簇催化剂的制备方法,包括以下制备步骤:Embodiment 1: a preparation method of carbon-supported metal nanocluster catalyst, comprising the following preparation steps:

1)将2g导电炭黑粉末浸泡至70mL食人鱼溶液中20h,随后用去离子水抽滤洗涤至最后的滤出液体的pH为7,制备得到富官能团碳载体粉末;1) Soak 2g of conductive carbon black powder into 70mL of piranha solution for 20h, then use deionized water to filter and wash until the pH of the final filtrate is 7, and prepare functional group-rich carbon carrier powder;

2)将0.5g富官能团碳载体粉末浸泡至20mL,0.05 mol/L的氯铂酸溶液中,在40℃下保温10h,吸附后进行冷冻干燥,制备得到金属吸附碳载体材料;2) Immerse 0.5 g of functional group-rich carbon carrier powder into 20 mL of 0.05 mol/L chloroplatinic acid solution, keep at 40 °C for 10 h, and freeze-dry after adsorption to prepare a metal-adsorbed carbon carrier material;

3)将金属吸附碳载体材料置于氩气环境中,在50℃下用正十二硫醇分子熏蒸处理10h,制备得到硫醇-金属-碳载体复合材料;3) The metal-adsorbed carbon support material was placed in an argon atmosphere, and fumigated with n-dodecanethiol molecules at 50 °C for 10 h to prepare a thiol-metal-carbon support composite material;

4)将硫醇-金属-碳载体复合材料在氩气气氛下,以5℃/min的升温速率升温至400℃,保温煅烧1h,制备得到碳负载金属纳米团簇催化剂。4) The thiol-metal-carbon support composite material was heated to 400 °C at a heating rate of 5 °C/min in an argon atmosphere, and calcined for 1 h to prepare a carbon-supported metal nanocluster catalyst.

实施例2:一种碳负载金属纳米团簇催化剂的制备方法,包括以下制备步骤:Embodiment 2: a preparation method of carbon-supported metal nanocluster catalyst, comprising the following preparation steps:

1)将3.5g活性炭浸泡至100mL食人鱼溶液中48h,随后用去离子水过滤洗涤至最后的滤出液体的pH为6,制备得到富官能团碳载体粉末;1) Soak 3.5g of activated carbon into 100mL of piranha solution for 48h, then filter and wash with deionized water until the pH of the final filtrate is 6, to prepare functional group-rich carbon carrier powder;

2)将富官能团碳载体粉末浸泡至5 mol/L的氯化铁溶液中,在25℃下保温20h,吸附后进行冷冻干燥,制备得到金属吸附碳载体材料;2) Immerse the functional group-rich carbon carrier powder in a 5 mol/L ferric chloride solution, keep at 25 °C for 20 hours, and freeze-dry it after adsorption to prepare a metal-adsorbed carbon carrier material;

3)将金属吸附碳载体材料置于氩气环境中,在10℃下用甲硫醇分子熏蒸处理100h,制备得到硫醇-金属-碳载体复合材料;3) The metal-adsorbed carbon support material was placed in an argon atmosphere, and fumigated with methyl mercaptan molecules at 10 °C for 100 h to prepare a thiol-metal-carbon support composite material;

4)将硫醇-金属-碳载体复合材料在氩气气氛下,以10℃/min的升温速率升温至700℃,保温煅烧2h,制备得到碳负载金属纳米团簇催化剂。4) The thiol-metal-carbon support composite material was heated to 700 °C at a heating rate of 10 °C/min in an argon atmosphere, and calcined for 2 h to prepare a carbon-supported metal nanocluster catalyst.

实施例3:一种碳负载金属纳米团簇催化剂的制备方法,包括以下制备步骤:Embodiment 3: a preparation method of carbon-supported metal nanocluster catalyst, comprising the following preparation steps:

1)将0.5g石墨烯浸泡至100mL食人鱼溶液中10h,随后用去离子水过滤洗涤至最后的滤出液体的pH为6.5,制备得到富官能团碳载体粉末;1) Soak 0.5 g of graphene in 100 mL of piranha solution for 10 hours, then filter and wash with deionized water until the pH of the final filtrate is 6.5, to prepare functional group-rich carbon carrier powder;

2)将富官能团碳载体粉末浸泡至0.005 mol/L的硝酸银溶液中,在99℃下保温5h,吸附后进行冷冻干燥,制备得到金属吸附碳载体材料;2) Immerse the functional group-rich carbon carrier powder in 0.005 mol/L silver nitrate solution, keep at 99 °C for 5 h, and freeze-dry after adsorption to prepare a metal-adsorbed carbon carrier material;

3)将金属吸附碳载体材料置于密闭真空环境或惰性气体环境中,在220℃下用环己硫醇分子熏蒸处理5h,制备得到硫醇-金属-碳载体复合材料;3) The metal-adsorbed carbon support material is placed in a closed vacuum environment or an inert gas environment, and fumigated with cyclohexanethiol molecules at 220 °C for 5 hours to prepare a thiol-metal-carbon support composite material;

4)将硫醇-金属-碳载体复合材料在氩气气氛下,以7℃/min的升温速率升温至300℃,保温煅烧4h,制备得到碳负载金属纳米团簇催化剂。4) The thiol-metal-carbon support composite material was heated to 300 °C at a heating rate of 7 °C/min in an argon atmosphere, and calcined for 4 h to prepare a carbon-supported metal nanocluster catalyst.

对实施例1制备得到的碳负载金属纳米团簇催化剂进行表征,结果如图所示。The carbon-supported metal nanocluster catalyst prepared in Example 1 was characterized, and the results are shown in the figure.

实施例1碳负载金属纳米团簇催化剂的TEM和暗场下STEM分别如图1和图2所示,从图1的TEM图谱可知,碳载体是由尺寸在20-80nm的石墨化碳球组成;而在高倍暗场STEM(如图2所示),可以看到碳载体上负载有金属纳米团簇的亮点,且该金属纳米团簇的尺寸在0.1-2nm之间,且分散度很好。Example 1 The TEM and dark field STEM of the carbon-supported metal nanocluster catalyst are shown in Figure 1 and Figure 2, respectively. From the TEM pattern in Figure 1, it can be seen that the carbon support is composed of graphitized carbon spheres with a size of 20-80 nm. ; and in the high-power dark-field STEM (as shown in Figure 2), the bright spots of metal nanoclusters loaded on the carbon support can be seen, and the size of the metal nanoclusters is between 0.1-2 nm and the dispersion is very good. .

实施例1碳负载金属纳米团簇催化剂XRD图谱如图3所示,图中并没有发现Pt金属的XRD特征峰,说明Pt颗粒的尺寸非常小。Example 1 The XRD pattern of the carbon-supported metal nanocluster catalyst is shown in Figure 3, and no XRD characteristic peaks of Pt metal are found in the figure, indicating that the size of the Pt particles is very small.

经测定,对实施例1的Pt的负载量为12.5%,并与Johon Matthey 型商业20%Pt/C催化剂的ORR催化性能进行对比,结果如图所示。图中可知,实施例1碳负载金属纳米团簇催化剂极限电流密度达5.35 mA·cm-2,同条件下测试的商业20%Pt/C催化剂的极限电流密度为5.52 mA·cm-2;但将其转化为Pt的质量活性,实施例1碳负载金属纳米团簇催化剂的活性是Johon Matthey 型商业20%Pt/C催化剂的1.55倍,很明显相对于商业催化剂提高的Pt的利用率,可有效降低燃料电池中Pt的使用量。It was determined that the loading amount of Pt in Example 1 was 12.5%, and the ORR catalytic performance was compared with that of the Johon Matthey type commercial 20% Pt/C catalyst. The results are shown in the figure. As can be seen from the figure, the limiting current density of the carbon-supported metal nanocluster catalyst in Example 1 reaches 5.35 mA·cm −2 , and the limiting current density of the commercial 20% Pt/C catalyst tested under the same conditions is 5.52 mA·cm −2 ; Converting it into the mass activity of Pt, the activity of the carbon-supported metal nanocluster catalyst in Example 1 is 1.55 times that of the Johon Matthey-type commercial 20% Pt/C catalyst. It is obvious that the improved Pt utilization compared with the commercial catalyst can be used. Effectively reduce the amount of Pt used in fuel cells.

Claims (8)

1. A preparation method of a carbon-supported metal nanocluster catalyst is characterized by comprising the following preparation steps:
1) soaking the carbon carrier into an acid treatment solution, and then filtering and washing to prepare carbon carrier powder rich in functional groups;
2) soaking the carbon carrier powder rich in functional groups into a soluble metal salt solution, and carrying out washing and freeze drying after adsorption to prepare a metal adsorption carbon carrier material;
3) putting the metal-adsorbed carbon carrier material into volatile mercaptan vapor for fumigation treatment to prepare a mercaptan-metal-carbon carrier composite material;
4) and calcining the mercaptan-metal-carbon carrier composite material under a protective atmosphere to prepare the carbon-supported metal nanocluster catalyst.
2. The method of claim 1, wherein the carbon support of step 1) comprises one or more of activated carbon, conductive carbon black, carbon paper, carbon cloth, and grapheme carbon material.
3. The method for preparing a carbon-supported metal nanocluster catalyst as recited in claim 1, wherein said acid treatment liquid of step 1) includes a piranha solution; the mass ratio of the carbon carrier powder to the acid treatment solution is 0.5-3.5: 100; the soaking time is 10-48 h; in the filtration washing, the filtrate is washed with deionized water until the pH of the final filtrate is between 6 and 7.
4. The method for preparing a carbon-supported metal nanocluster catalyst as recited in claim 1, wherein said soluble metal salt solution of step 2) comprises one or more mixed solution of Pt salt, Au salt, Ru salt, Rh salt, Fe salt, Co salt, Ni salt, Pd salt, Ag salt, and said soluble metal salt solution is 0.005-5 mol/L.
5. The method for preparing a carbon-supported metal nanocluster catalyst as recited in claim 1, wherein said step 2) is performed by mixing said functional group-rich carbon support powder with a soluble metal salt solution in a ratio of 0.1-3.5: 100; the soaking is carried out at 25-99 deg.C for 5-20 h.
6. The method for preparing a carbon-supported metal nanocluster catalyst according to claim 1, wherein the fumigating treatment in step 3) is carried out in a closed vacuum environment or an inert gas environment at 10-220 ℃ for 5-100 h.
7. The method for preparing a carbon-supported metal nanocluster catalyst as recited in claim 1, wherein said thiol of said step 3) comprises one or more of methyl mercaptan, ethyl mercaptan, octyl mercaptan, cyclohexyl mercaptan, cyclopentyl mercaptan, n-dodecyl mercaptan, 2-propyl mercaptan, heptyl mercaptan, phenethyl mercaptan, and butyl mercaptan.
8. The method for preparing a carbon-supported metal nanocluster catalyst as recited in claim 1, wherein the calcination in step 4) is performed by heating to 300-700 ℃ at a heating rate of 5-10 ℃/min, and maintaining the temperature for 1-4 h.
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