CN116995254A - Composite structure catalyst for synthesizing supported Pt-MXene and preparation method and application thereof - Google Patents

Composite structure catalyst for synthesizing supported Pt-MXene and preparation method and application thereof Download PDF

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CN116995254A
CN116995254A CN202311237976.6A CN202311237976A CN116995254A CN 116995254 A CN116995254 A CN 116995254A CN 202311237976 A CN202311237976 A CN 202311237976A CN 116995254 A CN116995254 A CN 116995254A
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mxene
platinum
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stirring
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夏昕
安世杰
杨鸿宇
徐超
叶锋
李远峰
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North China Electric Power University
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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
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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
    • H01M4/92Metals of platinum group
    • H01M4/925Metals of platinum group supported on carriers, e.g. powder carriers
    • H01M4/926Metals of platinum group supported on carriers, e.g. powder carriers on carbon or graphite

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Abstract

本发明涉及合成负载型Pt‑MXene复合结构催化剂及其制备方法与应用,属于电化学催化剂制备技术领域。本发明中合成负载型Pt‑MXene复合结构催化剂以MXene为载体,以铂为活性物质,所述铂均匀分散在所述MXene表面,所述铂包括以0价铂金属粒子为主的Pt0与Pt2+。本发明解决了现有技术中铂催化剂制备方法复杂、铂金属粒子尺寸大、稳定性差等技术问题。利用MXene载体与金属的界面强相互作用,获得均匀分散铂纳米粒子,MXene表面负载的铂颗粒大小可达到2nm以下,借由双金属的电子耦合效果提高铂催化活性;铂金属粒子与MXene间具有较强的金属‑载体界面相互作用,有利于提高催化剂的稳定性和分散性。

The invention relates to the synthesis of a supported Pt-MXene composite structure catalyst and its preparation method and application, and belongs to the technical field of electrochemical catalyst preparation. The synthetic supported Pt-MXene composite structure catalyst in the present invention uses MXene as the carrier and platinum as the active material. The platinum is evenly dispersed on the surface of the MXene. The platinum includes Pt 0 and 0-valent platinum metal particles. Pt 2+ . The invention solves the technical problems in the prior art such as complex preparation method of platinum catalyst, large size of platinum metal particles, and poor stability. Utilizing the strong interface interaction between the MXene carrier and the metal, uniformly dispersed platinum nanoparticles are obtained. The size of the platinum particles loaded on the surface of MXene can reach less than 2nm, and the platinum catalytic activity is improved by the electronic coupling effect of the bimetal; there is a strong interaction between the platinum metal particles and MXene. Strong metal-support interface interaction is beneficial to improving the stability and dispersion of the catalyst.

Description

一种合成负载型Pt-MXene复合结构催化剂及其制备方法与 应用A synthetic supported Pt-MXene composite structure catalyst and its preparation method and application

技术领域Technical field

本发明属于电化学催化剂制备技术领域,尤其涉及一种合成负载型Pt-MXene复合结构催化剂及其制备方法与应用。The invention belongs to the technical field of electrochemical catalyst preparation, and in particular relates to a synthetic supported Pt-MXene composite structure catalyst and its preparation method and application.

背景技术Background technique

开发高效稳定的负载型铂催化剂是推动质子交换膜燃料电池商业化应用的关键材料技术。常用的铂-碳催化剂受限于碳载体材料热稳定性差,铂原子比活性不足。寻找导电性好、耐腐蚀的非金属烯MXene作为一种新型二维材料,兼具金属和陶瓷的特性,表面活性位点多,有利于形成高分散性的铂分散结构,作为碳载体的取代物具有广泛的应用前景。将铂均匀分布在载体上是提高催化剂单位质量活性的极限,同时将催化科学带入到一个更小的研究尺度。The development of efficient and stable supported platinum catalysts is a key material technology to promote the commercial application of proton exchange membrane fuel cells. Commonly used platinum-carbon catalysts are limited by the poor thermal stability of the carbon support material and insufficient platinum atom specific activity. Looking for non-metallic alkenes with good conductivity and corrosion resistance, MXene, as a new two-dimensional material, has the characteristics of metals and ceramics, has many surface active sites, and is conducive to the formation of highly dispersible platinum dispersed structures, as a replacement for carbon carriers The material has broad application prospects. Evenly distributing platinum on the carrier is the ultimate limit for improving the activity per unit mass of the catalyst, and at the same time bringing catalysis science to a smaller research scale.

通常实现纳米级的铂催化结构需要原子层沉积(ALD)或化学气相沉积(CVD)。ALD方法虽然能够有效控制金属在基底表面的沉积形貌实现贵金属的纳米薄膜结构(4-5纳米),但是成本高、收率低、限制了其工业应用。CVD方法所需的沉积温度高(一般在900~2000°C之间),高温容易对材料造成损伤,限制了衬底和沉积层的选择,且参与沉积反应的气源和反应后的余气都有一定的毒性,存在安全隐患。Usually achieving nanoscale platinum catalytic structures requires atomic layer deposition (ALD) or chemical vapor deposition (CVD). Although the ALD method can effectively control the deposition morphology of metal on the substrate surface to achieve a nanometer thin film structure (4-5 nanometers) of precious metals, its high cost and low yield limit its industrial application. The CVD method requires high deposition temperatures (generally between 900 and 2000°C). High temperatures can easily cause damage to materials, limiting the selection of substrates and deposition layers, as well as the gas sources involved in the deposition reaction and the residual gas after the reaction. They all have a certain degree of toxicity and pose safety risks.

公开于该背景技术部分的信息仅仅旨在增加对本发明的总体背景的理解,而不应当被视为承认或以任何形式暗示该信息构成已为本领域一般技术人员所公知的现有技术。The information disclosed in this Background section is merely intended to enhance an understanding of the general background of the invention and should not be construed as an admission or in any way implying that the information constitutes prior art that is already known to a person of ordinary skill in the art.

发明内容Contents of the invention

为了解决现有技术中铂催化剂制备方法复杂、反应温度高、能耗大、存在安全隐患,且铂金属粒子尺寸大,分散性、稳定性差的技术问题,提供一种合成负载型Pt-MXene复合结构催化剂及其制备方法与应用。In order to solve the technical problems in the existing technology that the platinum catalyst preparation method is complicated, the reaction temperature is high, the energy consumption is high, there are safety hazards, and the platinum metal particles are large in size and have poor dispersion and stability, a synthetic supported Pt-MXene composite is provided Structural catalysts and their preparation methods and applications.

本申请第一方面提供一种合成负载型Pt-MXene复合结构催化剂,所述催化剂以MXene为载体,以铂为活性物质,所述铂均匀分散在所述MXene表面,所述铂包括0价铂金属粒子(Pt0)与Pt2+The first aspect of this application provides a synthetic supported Pt-MXene composite structure catalyst. The catalyst uses MXene as a carrier and platinum as an active material. The platinum is evenly dispersed on the surface of the MXene. The platinum includes zero-valent platinum. Metal particles (Pt 0 ) and Pt 2+ .

MXene表面形成的铂原子(铂的0价金属粒子)与Pt2+有较强的界面相互作用,有利于提高催化剂的稳定性和分散性。The platinum atoms (0-valent metal particles of platinum) formed on the surface of MXene have strong interfacial interaction with Pt 2+ , which is beneficial to improving the stability and dispersion of the catalyst.

在一些实施方式中,所述0价铂金属粒子的粒径为1~5nm;In some embodiments, the particle size of the zero-valent platinum metal particles is 1 to 5 nm;

和/或,所述MXene表面的0价铂金属粒子占总的Pt含量的70%以上。And/or, the 0-valent platinum metal particles on the surface of the MXene account for more than 70% of the total Pt content.

在一些实施方式中,所述0价铂金属粒子的粒径可达到2nm以下。In some embodiments, the particle size of the zero-valent platinum metal particles can reach 2 nm or less.

本发明第二方面提供一种上述合成负载型Pt-MXene复合结构催化剂的制备方法,所述制备方法采用乙二醇还原浸渍法,包括:A second aspect of the present invention provides a method for preparing the above-mentioned synthetic supported Pt-MXene composite structure catalyst. The preparation method adopts an ethylene glycol reduction impregnation method, including:

步骤S1:将MXene加入到尿素水溶液中,超声混合均匀后,加入氯铂酸,搅拌混合后加热反应,反应后冷却至室温,得到混合溶液;Step S1: Add MXene to the urea aqueous solution, mix evenly with ultrasonic, add chloroplatinic acid, stir and mix, then heat the reaction, cool to room temperature after the reaction, and obtain a mixed solution;

步骤S2:将乙二醇加入到步骤S1得到混合溶液中,混合搅拌后加热,加热结束后继续搅拌,经过后处理后得到合成负载型Pt-MXene复合结构催化剂。Step S2: Add ethylene glycol to the mixed solution obtained in step S1, mix and stir, then heat, continue stirring after heating, and obtain a synthetic supported Pt-MXene composite structure catalyst after post-processing.

在一些实施方式中,所述后处理的包括过滤、用去离子水洗涤,洗涤3次。In some embodiments, the post-processing includes filtration, washing with deionized water, and washing three times.

在一些实施方式中,所述MXene为第IIIB-VIB族金属碳化物。In some embodiments, the MXene is a Group IIIB-VIB metal carbide.

在一些实施方式中,所述MXene为Mo2CTx、Ti3C2Tx、V2CTx、Nb2CTx和Cr2CTx中的一种,优选的,所述MXene为Mo2CTx或Ti3C2Tx。In some embodiments, the MXene is one of Mo 2 CTx , Ti 3 C 2 Tx, V 2 CTx, Nb 2 CTx and Cr 2 CTx. Preferably, the MXene is Mo 2 CTx or Ti 3 C 2 Tx.

刻蚀掉的A位金属均为Al或G。The etched A-site metal is all Al or G.

在一些实施方式中,所述MXene的制备方法包括:将前驱体MAX于刻蚀溶液中超声处理后,发生刻蚀反应,洗涤干燥后,得到MXene。In some embodiments, the preparation method of MXene includes: ultrasonically treating the precursor MAX in an etching solution, causing an etching reaction, and washing and drying to obtain MXene.

当MXene为Mo2CTx时,其前驱体MAX为Mo2Al2C或Mo2Ga2C;When MXene is Mo 2 CT x , its precursor MAX is Mo 2 Al 2 C or Mo 2 Ga 2 C;

当MXene为Ti3C2Tx时,其前驱体MAX为Ti3AlC2或Ti3GaC2When MXene is Ti 3 C 2 Tx, its precursor MAX is Ti 3 AlC 2 or Ti 3 GaC 2 ;

当MXene为V2CTx时,其前驱体MAX为V2AlC或V2GaC;When MXene is V 2 CTx, its precursor MAX is V 2 AlC or V 2 GaC;

当MXene为Nb2CTx时,其前驱体MAX为Nb2AlC或Nb2GaC;When MXene is Nb 2 CTx, its precursor MAX is Nb 2 AlC or Nb 2 GaC;

当MXene为Cr2CTx时,其前驱体MAX为Cr2AlC/Cr2GaC。When MXene is Cr 2 CTx, its precursor MAX is Cr 2 AlC/Cr 2 GaC.

在一些实施方式中,所述刻蚀溶液为盐酸与氟化铵的混合溶液,所述盐酸的浓度为30~60wt%,所述氟化铵与所述MAX的质量比为1:1;In some embodiments, the etching solution is a mixed solution of hydrochloric acid and ammonium fluoride, the concentration of the hydrochloric acid is 30~60wt%, and the mass ratio of the ammonium fluoride to the MAX is 1:1;

和/或,所述超声处理的时间为30~60 min;And/or, the ultrasonic treatment time is 30~60 minutes;

和/或,所述刻蚀反应的温度为140℃~160℃,所述刻蚀反应的时间为12-24 h。And/or, the temperature of the etching reaction is 140°C~160°C, and the time of the etching reaction is 12-24 h.

氟化铵与盐酸间接的形成HF,用来刻蚀基底,相比于直接使用HF进行刻蚀,反应更加稳定,安全性更高。Ammonium fluoride and hydrochloric acid indirectly form HF, which is used to etch the substrate. Compared with directly using HF for etching, the reaction is more stable and safer.

在一些实施方式中,所述步骤S1中尿素水溶液中尿素的质量与水的体积比为(300~400)mg/(200~300)ml;In some embodiments, the volume ratio of the mass of urea to water in the urea aqueous solution in step S1 is (300~400) mg/(200~300) ml;

和/或,所述步骤S1中所述氯铂酸的浓度为0.05M;And/or, the concentration of chloroplatinic acid in step S1 is 0.05M;

和/或,所述步骤S1中搅拌为机械搅拌,机械搅拌的时间为3~4h,或,所述步骤S1中搅拌为超声搅拌,超声搅拌时间为30~60min;And/or, the stirring in step S1 is mechanical stirring, and the mechanical stirring time is 3 to 4 hours; or, the stirring in step S1 is ultrasonic stirring, and the ultrasonic stirring time is 30 to 60 minutes;

和/或,所述步骤S1中加热的温度为90~100℃,加热的时间为1~2h;And/or, the heating temperature in step S1 is 90~100°C, and the heating time is 1~2h;

和/或,所述步骤S2中所述乙二醇与所述混合溶液的体积比为1:1~1:1.5;And/or, the volume ratio of the ethylene glycol and the mixed solution in step S2 is 1:1~1:1.5;

和/或,所述步骤S2中混合搅拌为机械搅拌,机械搅拌的时间为3~4h,或,所述步骤S2中混合搅拌为超声搅拌,超声搅拌时间为30~60min;And/or, the mixing and stirring in step S2 is mechanical stirring, and the mechanical stirring time is 3 to 4 hours; or, the mixing and stirring in step S2 is ultrasonic stirring, and the ultrasonic stirring time is 30 to 60 minutes;

和/或,所述步骤S2中加热的温度为120~130℃,加热时间为1~2h;And/or, the heating temperature in step S2 is 120~130°C, and the heating time is 1~2h;

和/或,所述步骤S2中加热结束后继续搅拌的时间为12~14h。And/or, the time for continuing stirring after heating in step S2 is 12 to 14 hours.

在90℃以上,尿素在氯铂酸溶液中水解产生OH-,在溶液中均匀分布OH-,从而避免了pH的突然升高而形成Pt的氢氧化物的沉淀;控制温度不超过100℃是为了较少资源浪费,同时,使得水解反应能够缓慢的进行。Above 90°C, urea is hydrolyzed in chloroplatinic acid solution to produce OH - , which is evenly distributed in the solution, thereby avoiding the sudden increase in pH and the formation of Pt hydroxide precipitation; controlling the temperature not to exceed 100° C is In order to reduce the waste of resources, at the same time, the hydrolysis reaction can be carried out slowly.

由于乙二醇的存在,在升温超过100℃后产生乙醛,从而能够还原已经形成的Pt的高价化合物,形成Pt的金属粒子,若温度未到达100℃,还原剂不能够有效作用,温度太高使得反应速率过快造成Pt颗粒的聚集。Due to the presence of ethylene glycol, acetaldehyde is generated when the temperature exceeds 100°C, which can reduce the high-priced Pt compounds that have been formed to form Pt metal particles. If the temperature does not reach 100°C, the reducing agent cannot effectively act and the temperature is too high. High makes the reaction rate too fast and causes the aggregation of Pt particles.

本发明第三方面提供一种上述合成负载型Pt-MXene复合结构催化剂或上述制备方法制备得到的合成负载型Pt-MXene复合结构催化剂作为质子交换膜燃料电池氧还原催化剂、水电解析氧催化剂或二氧化碳电还原催化剂的应用。The third aspect of the present invention provides the above-mentioned synthetic supported Pt-MXene composite structure catalyst or the synthetic supported Pt-MXene composite structure catalyst prepared by the above-mentioned preparation method as a proton exchange membrane fuel cell oxygen reduction catalyst, hydroelectric oxygen desorption catalyst or carbon dioxide Applications of electroreduction catalysts.

相比于现有技术,本发明达到的技术效果如下:Compared with the existing technology, the technical effects achieved by the present invention are as follows:

(1)本发明的合成负载型Pt-MXene结构单原子铂催化剂采用乙二醇还原方法(湿化学方法),选用Mo2CTx、Ti3C2Tx等MXene二维材料作为二维载体和共催化剂,反应后,MXene载体表面不仅负载了0价铂金属粒子,还负载有Pt2+,其中0价铂金属粒子可达70%以上,一方面利用MXene载体与金属的界面强相互作用,获得均匀分散铂纳米粒子,通过对合成材料表征得到的MXene表面负载的铂颗粒大小可达到2nm以下,并借由双金属的电子耦合效果提高铂的催化活性;另一方面,Pt2+与铂0价金属原子间具有较强的界面相互作用,有利于提高催化剂的稳定性和分散性。(1) The synthetic supported Pt-MXene structure single-atom platinum catalyst of the present invention adopts the ethylene glycol reduction method (wet chemical method), and selects MXene two-dimensional materials such as Mo 2 CT x and Ti 3 C 2 T x as the two-dimensional carrier. and co-catalyst, after the reaction, the surface of the MXene carrier is not only loaded with 0-valent platinum metal particles, but also loaded with Pt 2+ , of which 0-valent platinum metal particles can reach more than 70%. On the one hand, the strong interface interaction between the MXene carrier and the metal is used , to obtain uniformly dispersed platinum nanoparticles. The size of platinum particles loaded on the surface of MXene obtained through characterization of synthetic materials can reach less than 2nm, and the catalytic activity of platinum is improved by the electronic coupling effect of bimetals; on the other hand, Pt 2+ and Platinum zero-valent metal atoms have strong interfacial interactions, which is beneficial to improving the stability and dispersion of the catalyst.

(2)本发明采用还原的方式制得的催化剂材料,此工艺方法相对于传统的原子层沉积等工艺相比较,工艺较为简单,合成周期短,相对于CVD合成方法反应温度更低,避免了资源浪费的同时也提高了实验的安全性。(2) The present invention uses catalyst materials prepared by reduction. Compared with traditional atomic layer deposition and other processes, this process is simpler, the synthesis cycle is short, and the reaction temperature is lower than the CVD synthesis method, which avoids This waste of resources also improves the safety of the experiment.

(3)本发明中采用尿素和乙二醇还原方法在现有技术中对MXene-TM合成方法中还未提及,利用合成Pt-MXene催化剂的均匀的纳米粒子的分布和良好的导电协同作用,利用Ti3C2Tx、Mo2CTx等二维材料的二维高表面独特的化学结构,可以实现Pt纳米粒子在MXene二维材料边缘的均匀分散,从TEM图中可清晰的看出合成的Pt/MXene在表面形貌上趋近于单原子级分散,可达到2nm以下,实现稳定的铂催化结构,有利于提高-电催化剂催化性能。(3) The urea and ethylene glycol reduction method used in the present invention has not been mentioned in the MXene-TM synthesis method in the prior art. The uniform nanoparticle distribution and good conductive synergy of the synthesized Pt-MXene catalyst are utilized. , using the unique chemical structure of the two-dimensional high surface of two-dimensional materials such as Ti 3 C 2 T x and Mo 2 CT It is found that the surface morphology of the synthesized Pt/MXene is close to single-atom level dispersion, which can reach less than 2 nm, achieving a stable platinum catalytic structure, which is beneficial to improving the catalytic performance of electrocatalysts.

(4)本发明采用的湿化学合成方法具有工艺简单、成本低、反应温度低、安全可靠,便于大规模工业生产的优点,合成MXene的制备过程相对于HF刻蚀方法较为简单安全;本发明的实验方法同时适用于MXene衬底上非贵金属催化剂单原子结构的制备,能够得到更广泛的应用。(4) The wet chemical synthesis method adopted in the present invention has the advantages of simple process, low cost, low reaction temperature, safety and reliability, and is convenient for large-scale industrial production. The preparation process of synthesizing MXene is simpler and safer than the HF etching method; the present invention The experimental method is also suitable for the preparation of single-atom structures of non-noble metal catalysts on MXene substrates, and can be used more widely.

附图说明Description of the drawings

图1是本发明实施例1中刻蚀后制备得到的Mo2CTx二维材料SEM图;Figure 1 is an SEM image of the Mo 2 CT x two-dimensional material prepared after etching in Example 1 of the present invention;

图2是本发明实施例1中刻蚀后Mo2CTx的XRD表征图与Pt/Mo2CTx复合材料XRD图;Figure 2 is the XRD characterization diagram of Mo 2 CT x after etching and the XRD diagram of Pt/Mo 2 CT x composite material in Example 1 of the present invention;

图3是本发明实施例1中Pt/Mo2CTx复合材料XPS图,其中(a)为全谱图,(b)为铂的分峰谱图;Figure 3 is an XPS chart of the Pt/Mo 2 CT x composite material in Example 1 of the present invention, in which (a) is the full spectrum and (b) is the split-peak spectrum of platinum;

图4是本发明实施例1中Pt/Mo2CTx复合材料的TEM、EDS图及粒径分布图,其中(a)和(c)为Pt/Mo2CTx的TEM表征图,(b)为Pt/Mo2CTx的EDS表征图,(d)为Pt/Mo2CTx的粒径分布图;Figure 4 is the TEM, EDS pictures and particle size distribution diagram of the Pt/Mo 2 CT x composite material in Example 1 of the present invention, where (a) and (c) are the TEM characterization pictures of Pt/Mo 2 CT x , (b ) is the EDS characterization diagram of Pt/Mo 2 CT x , (d) is the particle size distribution diagram of Pt/Mo 2 CT x ;

图5为本发明实施例2中Pt/Mo2CTx复合材料的TEM及EDS图,其中(a)为Pt/Mo2CTx的TEM表征图,(b)为Pt/Mo2CTx的EDS表征图;Figure 5 is the TEM and EDS images of the Pt/Mo 2 CT x composite material in Example 2 of the present invention, where (a) is the TEM characterization image of Pt/Mo 2 CT x , and (b) is the Pt/Mo 2 CT x EDS characterization diagram;

图6为本发明实施例3中Pt/Ti3C2Tx复合材料的TEM、EDS及粒径分布图,其中(a)为Pt/Ti3C2Tx的TEM表征图,(b)为Pt/Ti3C2Tx的EDS表征图,(c)为Pt/Ti3C2Tx的粒径分布图;Figure 6 shows the TEM, EDS and particle size distribution diagrams of the Pt/Ti 3 C 2 T x composite material in Example 3 of the present invention, where (a) is the TEM characterization diagram of Pt/Ti 3 C 2 T x , and (b) is the EDS characterization diagram of Pt/Ti 3 C 2 T x , (c) is the particle size distribution diagram of Pt/Ti 3 C 2 T x ;

图7为发明实施例1、实施例2制得的Pt/Mo2CTx复合材料、Mo2CTX和Pt/C电化学性能测试中的LSV对比图;Figure 7 is a LSV comparison chart in the electrochemical performance test of Pt/Mo 2 CT x composite materials, Mo 2 CT X and Pt/C prepared in Example 1 and Example 2 of the invention;

图8为本发明对比例1制得的复合材料的SEM和EDS表征图,其中(a)为SEM图,(b)为EDS图;Figure 8 is the SEM and EDS characterization images of the composite material prepared in Comparative Example 1 of the present invention, where (a) is the SEM image and (b) is the EDS image;

图9为本发明对比例2制得的复合材料的EDS表征图,其中(a)为该复合材料的EDS图,(b)为复合材料中Pt元素的EDS图;Figure 9 is an EDS characterization diagram of the composite material prepared in Comparative Example 2 of the present invention, where (a) is the EDS diagram of the composite material, and (b) is the EDS diagram of the Pt element in the composite material;

图10为本发明对比例3制得的复合材料的TEM图。Figure 10 is a TEM image of the composite material prepared in Comparative Example 3 of the present invention.

具体实施方式Detailed ways

以下结合附图通过具体实施例说明本发明的技术方案。应该理解,本发明提到的一个或者多个步骤不排斥在组合步骤前后还存在其他方法和步骤,或者这些明确提及的步骤间还可以插入其他方法和步骤。还应理解,这些实例仅用于说明本发明而不用于限制本发明的范围。除非另有说明,各方法步骤的编号仅为鉴别各方法步骤的目的,而非限制每个方法的排列次序或限定本发明的实施范围,其相对关系的改变或调整,在无实质技术内容变更的条件下,亦可视为本发明可实施的范畴。The technical solutions of the present invention will be described below through specific embodiments in conjunction with the accompanying drawings. It should be understood that the mention of one or more steps in the present invention does not exclude the existence of other methods and steps before and after the combination step, or that other methods and steps can be inserted between these explicitly mentioned steps. It should also be understood that these examples are merely illustrative of the invention and are not intended to limit the scope of the invention. Unless otherwise stated, the numbering of each method step is only for the purpose of identifying each method step, and does not limit the order of each method or limit the implementation scope of the present invention. Changes or adjustments in their relative relationships will not change the technical content without substantial changes. Under the conditions, it can also be regarded as the implementable scope of the present invention.

实施例中所采用的原料和仪器,对其来源没有特定限制,在市场购买或者按照本领域内技术人员熟知的常规方法制备即可。There are no specific restrictions on the sources of the raw materials and instruments used in the examples. They can be purchased in the market or prepared according to conventional methods well known to those skilled in the art.

在一些实施方式中,一种合成负载型Pt-MXene复合结构催化剂及制备方法,包括:In some embodiments, a synthetic supported Pt-MXene composite structure catalyst and preparation method include:

步骤1:取300~400 mg尿素溶于200~300 mL的去离子水,MXene加入到溶液里面,超声30~40 min。尿素用来缓慢调节溶液的pH值辅助沉积,在90℃以上,尿素在铂酸溶液中水解产生OH-,在溶液中均匀分布OH-,从而避免了pH的突然升高而形成Pt的氢氧化物的沉淀。Step 1: Dissolve 300~400 mg of urea in 200~300 mL of deionized water, add MXene to the solution, and sonicate for 30~40 minutes. Urea is used to slowly adjust the pH value of the solution to assist deposition. Above 90°C, urea is hydrolyzed in the platinum acid solution to produce OH - , and OH - is evenly distributed in the solution, thus avoiding the sudden rise in pH and the formation of Pt hydroxide. precipitation of matter.

步骤2:将氯铂酸溶液加入到步骤1混合好的溶液中,搅拌3~4h,然后将混合物于90~100℃下加热1~2h,冷却到室温,得到混合溶液。Step 2: Add the chloroplatinic acid solution to the mixed solution in step 1, stir for 3 to 4 hours, then heat the mixture at 90 to 100°C for 1 to 2 hours, and cool to room temperature to obtain a mixed solution.

步骤3:200~230 ml乙二醇加入到步骤2已经冷却到室温的混合溶液中,搅拌3~4h,120~130℃加热1 h,然后搅拌10~12h。由于乙二醇的存在,在升温超过100摄氏度后产生乙醛,从而能够还原已经形成的Pt的化合物,形成Pt的金属粒子。从后面附图的XPS图中可以清晰的看到Pt0金属粒子和Pt2+生成。在此步骤中,若温度未到达100℃,还原剂不能够有效作用,温度太高使得反应速率过快造成Pt颗粒的聚集。Step 3: Add 200~230 ml of ethylene glycol to the mixed solution that has been cooled to room temperature in Step 2, stir for 3~4 hours, heat at 120~130°C for 1 hour, and then stir for 10~12 hours. Due to the presence of ethylene glycol, acetaldehyde is generated when the temperature exceeds 100 degrees Celsius, which can reduce the Pt compounds that have been formed to form Pt metal particles. From the XPS picture in the following figure, you can clearly see the generation of Pt 0 metal particles and Pt 2+ . In this step, if the temperature does not reach 100°C, the reducing agent cannot effectively act. If the temperature is too high, the reaction rate will be too fast, resulting in the aggregation of Pt particles.

步骤4:过滤,洗涤,60~80℃干燥12~14h,得到合成负载型Pt-MXene复合铂催化剂。Step 4: Filter, wash, and dry at 60~80°C for 12~14 hours to obtain a synthetic supported Pt-MXene composite platinum catalyst.

实施例1:Pt/Mo2CTx Example 1: Pt/Mo 2 CT x

(1)MXene的制备:(1) Preparation of MXene:

将氟化铵2 g与40 mL 6M的盐酸溶液(11.8 mol/L)超声混合30 min,得到刻蚀溶液;然后将2 g MAX(Mo2Ga2C)浸渍入刻蚀溶液,再将混合溶液加入到100 ml容量的特氟隆内衬不锈钢反应釜中,升温至140 ℃,持续加热24 h,最后冷却到室温。将混合溶液用去离子水清洗和离心,直至pH值到6,然后用乙醇清洗3次,最后将得到的粉末60 ℃干燥12 h,得到Mo2CTx二维材料。Ultrasonically mix 2 g of ammonium fluoride and 40 mL of 6M hydrochloric acid solution (11.8 mol/L) for 30 minutes to obtain an etching solution; then immerse 2 g of MAX (Mo 2 Ga 2 C) into the etching solution, and then mix The solution was added to a Teflon-lined stainless steel reactor with a capacity of 100 ml, heated to 140°C, continued heating for 24 h, and finally cooled to room temperature. The mixed solution was washed and centrifuged with deionized water until the pH value reached 6, then washed three times with ethanol, and finally the obtained powder was dried at 60°C for 12 h to obtain Mo 2 CT x two-dimensional material.

(2)Pt/Mo2CTx的制备(2) Preparation of Pt/Mo 2 CT x

将300mg尿素溶于200mL的去离子水,60mg Mo2CTx加入到溶液里面,超声30 min。5mL 0.05M的H2PtCl6·6H2O加入到溶液中(氯铂酸和Mo2CTx的摩尔比为1:1),超声搅拌10-20min,然后将混合物90℃加热1h,冷却到室温。200ml乙二醇加入到溶液中,搅拌3h,120℃加热1h,然后搅拌12h。过滤,洗涤,80℃干燥12h,得到Pt/Mo2CTx复合材料,铂纳米粒子的粒径分布为2-5nm。Dissolve 300mg urea in 200mL deionized water, add 60mg Mo 2 CT x to the solution, and sonicate for 30 minutes. 5mL of 0.05M H 2 PtCl 6 ·6H 2 O was added to the solution (the molar ratio of chloroplatinic acid and Mo 2 CT room temperature. Add 200 ml of ethylene glycol to the solution, stir for 3 hours, heat at 120°C for 1 hour, and then stir for 12 hours. Filter, wash, and dry at 80°C for 12 hours to obtain a Pt/Mo 2 CT x composite material. The particle size distribution of platinum nanoparticles is 2-5 nm.

实施例2:Pt/Mo2CTx Example 2: Pt/Mo 2 CT x

本实施例中0.05 M H2PtCl6·6H2O加入量为1ml(氯铂酸和Mo2CTx的摩尔比为1:5),其他与实施例1相同。得到Pt/Mo2CTx复合材料,Pt金属粒子在Mo2CTx表面呈原子级均匀分散,粒径可达到2nm以下。In this example, the added amount of 0.05 MH 2 PtCl 6 ·6H 2 O is 1 ml (the molar ratio of chloroplatinic acid and Mo 2 CT x is 1:5), and the others are the same as in Example 1. A Pt/Mo 2 CT x composite material is obtained. Pt metal particles are evenly dispersed at the atomic level on the surface of Mo 2 CTx, and the particle size can reach less than 2 nm.

实施例3:Pt/Ti3C2Tx的制备Example 3: Preparation of Pt/Ti 3 C 2 Tx

(1)MXene的制备:(1) Preparation of MXene:

将氟化铵2 g与40 mL 6M的盐酸溶液(11.8 mol/L)超声混合30 min,得到刻蚀溶液;然后将2 g MAX(Ti3AlC2)浸渍入刻蚀溶液,再将混合溶液加入到100 ml容量的特氟隆内衬不锈钢反应釜中,升温至140 ℃,持续加热24 h,最后冷却到室温。将混合溶液用去离子水清洗和离心,直至pH值到6,然后用乙醇清洗3次,最后将得到的粉末60 ℃干燥12 h,得到Ti3C2Tx二维材料。Ultrasonically mix 2 g of ammonium fluoride and 40 mL of 6M hydrochloric acid solution (11.8 mol/L) for 30 minutes to obtain an etching solution; then immerse 2 g of MAX (Ti 3 AlC 2 ) into the etching solution, and then mix the mixed solution Add it to a Teflon-lined stainless steel reactor with a capacity of 100 ml, raise the temperature to 140°C, continue heating for 24 h, and finally cool to room temperature. The mixed solution was washed and centrifuged with deionized water until the pH value reached 6, then washed three times with ethanol, and finally the obtained powder was dried at 60°C for 12 h to obtain Ti 3 C 2 T x two-dimensional material.

(2)Pt/Ti3C2Tx的制备(2) Preparation of Pt/Ti 3 C 2 T x

将600 mg尿素溶于400 mL的去离子水,65 mg Ti3C2Tx加入到溶液里面,超声30min。5 mL 0.05M H2PtCl6·6H2O 加入到溶液中,搅拌3 h,然后将混合物加热至90 ℃,加热1 h,冷却到室温。200 ml 乙二醇加入到溶液中,搅拌3 h,120 ℃加热1 h,然后搅拌12 h。过滤,洗涤,80 ℃干燥12 h,得到Pt/Ti3C2Tx复合材料。Pt纳米粒子的粒径分布为2-5nm。Dissolve 600 mg of urea in 400 mL of deionized water, add 65 mg of Ti 3 C 2 T x to the solution, and sonicate for 30 minutes. 5 mL 0.05MH 2 PtCl 6 ·6H 2 O was added to the solution, stirred for 3 h, then the mixture was heated to 90 °C, heated for 1 h, and cooled to room temperature. 200 ml of ethylene glycol was added to the solution, stirred for 3 h, heated at 120°C for 1 h, and then stirred for 12 h. Filter, wash, and dry at 80°C for 12 hours to obtain Pt/Ti 3 C 2 T x composite material. The particle size distribution of Pt nanoparticles is 2-5nm.

产品表征与分析Product Characterization and Analysis

(1)实施例1中Mo2CTx二维材料SEM分析(1) SEM analysis of Mo 2 CT x two-dimensional material in Example 1

对实施例1中制得的Mo2CTx二维材料进行SEM分析,如图1所示,可以看到,刻蚀后的Mo2CTx是呈现多层状,能够增大催化剂的接触面积,提高催化剂的催化活性。SEM analysis was performed on the Mo 2 CT x two-dimensional material prepared in Example 1. As shown in Figure 1, it can be seen that the etched Mo 2 CT x is multi-layered, which can increase the contact area of the catalyst. , improve the catalytic activity of the catalyst.

(2)实施例1中Mo2CTx与Pt/Mo2CTx复合材料的XRD分析(2) XRD analysis of Mo 2 CTx and Pt/Mo 2 CT x composite materials in Example 1

对实施例1制得的Mo2CTx二维材料和Pt/Mo2CTx进行XRD分析,结果如图2所示,图上有各个组分的衍射峰,表明制备MXene步骤中,成功刻蚀得到Mo2CTx二维材料,经乙二醇还原后,Pt纳米粒子有效附载在Mo2CTx表面。 XRD analysis was performed on the Mo 2 CT The Mo 2 CTx two-dimensional material is obtained by etching. After reduction with ethylene glycol, Pt nanoparticles are effectively attached to the surface of Mo 2 CTx .

(3)实施例1中Pt/Mo2CTx复合材料的XPS、TEM、EDS及粒度分布分析(3) XPS, TEM, EDS and particle size distribution analysis of the Pt/Mo 2 CT x composite material in Example 1

如图3所示,在XPS表征图中可以清晰的看到Pt的0价金属粒子占总的Pt的化合物的70%以上,并有Pt2+;从图4可以看出可以很明显的看到单原子Pt在Mo2CTx表面沉积,并且分布均匀,纳米颗粒大小在2nm左右。As shown in Figure 3, it can be clearly seen in the XPS characterization chart that the 0-valent metal particles of Pt account for more than 70% of the total Pt compounds, and there are Pt 2+ ; as can be seen from Figure 4, it can be clearly seen that Single-atom Pt is deposited on the surface of Mo 2 CT x and is evenly distributed, with the nanoparticle size being about 2nm.

(4)实施例2中Pt/Mo2CTx复合材料的TEM及EDS分析(4) TEM and EDS analysis of Pt/Mo 2 CT x composite material in Example 2

如图5所示,从图中可以很明显的看到Pt在Mo2CTx表面呈原子级分散Pt纳米颗粒均匀分布,Pt颗粒大小在2nm以下。As shown in Figure 5, it can be clearly seen from the figure that Pt is evenly distributed in the form of atomically dispersed Pt nanoparticles on the surface of Mo 2 CT x , and the size of the Pt particles is below 2 nm.

(5)实施例3中Pt/Ti3C2Tx复合材料的TEM、EDS及粒径分布分析(5) TEM, EDS and particle size distribution analysis of the Pt/Ti 3 C 2 T x composite material in Example 3

如图6所示,从图中可以很明显的看到2nm左右的Pt颗粒在Ti3C2Tx表面均匀分布,证明了本发明提供的合成方法对多种MXene基底均适用。As shown in Figure 6, it can be clearly seen from the figure that Pt particles of about 2 nm are evenly distributed on the surface of Ti 3 C 2 Tx, which proves that the synthesis method provided by the present invention is applicable to a variety of MXene substrates.

(6)实施例1、实施例2中Pt/Mo2CTx复合材料的电化学性能测试(6) Electrochemical performance test of Pt/Mo 2 CT x composite materials in Example 1 and Example 2

利用氧气饱和0.1 M KOH电解液,参比电极是汞氧化汞电极,碳棒为对电极。2 mg科琴黑、20 mg样品、260 μL异丙醇、200 μL乙醇和40μL 5%的Nafion溶液混合到一起,冰浴超声40 min,取10 μL催化剂ink,旋凃于玻碳电极上,得到催化剂膜。然后利用旋转圆盘电极进行电化学性能测试。得到的LSV图如图7所示,实施例1制得的Pt/Mo2CTx复合材料的起始电势和半波电势分别为1.04V和0.87V,优于商用铂碳Pt电极,拥有良好的ORR(电催化氧还原反应)催化效果。Oxygen-saturated 0.1 M KOH electrolyte was used, the reference electrode was a mercury oxide electrode, and the carbon rod was the counter electrode. Mix 2 mg Ketjen Black, 20 mg sample, 260 μL isopropyl alcohol, 200 μL ethanol and 40 μL 5% Nafion solution together, sonicate in an ice bath for 40 min, take 10 μL catalyst ink, and spin-coat it on the glassy carbon electrode. A catalyst film was obtained. Rotating disk electrodes were then used for electrochemical performance testing. The obtained LSV diagram is shown in Figure 7. The starting potential and half-wave potential of the Pt/Mo 2 CT x composite material prepared in Example 1 are 1.04V and 0.87V respectively, which is better than the commercial platinum carbon Pt electrode and has good ORR (electrocatalytic oxygen reduction reaction) catalytic effect.

对比例1Comparative example 1

对比例1与实施例1的区别在于未加入尿素,其他与实施例1相同。The difference between Comparative Example 1 and Example 1 is that no urea was added, and the rest is the same as Example 1.

对比例制得的复合材料进行SEM表征和EDS表征,如图8所示,可以看到贵金属的沉积效果很不理想,Pt颗粒聚集在一起且沉积量很少,Pt的表面含量较低仅3%。SEM characterization and EDS characterization were performed on the composite materials prepared in the comparative example. As shown in Figure 8, it can be seen that the deposition effect of precious metals is very unsatisfactory. Pt particles gather together and the deposition amount is very small. The surface content of Pt is as low as only 3 %.

对比例2Comparative example 2

对比例2与实施例1的区别在于未加入乙二醇,其他与实施例1相同。The difference between Comparative Example 2 and Example 1 is that ethylene glycol was not added, and the others were the same as Example 1.

对比例制得的复合材料进行SEM表征和EDS表征,如图9所示,可以看到MXene表面沉积Pt金属颗粒粒径分布较不均匀,有部分较大的纳米颗粒。The composite material prepared in the comparative example was characterized by SEM and EDS. As shown in Figure 9, it can be seen that the particle size distribution of Pt metal particles deposited on the MXene surface is relatively uneven, and there are some larger nanoparticles.

对比例3Comparative example 3

对比例3与实施例1的区别在于未加未加入乙二醇,添加NaBH4还原剂,其它与实施例1相同。The difference between Comparative Example 3 and Example 1 is that no ethylene glycol was added, NaBH 4 reducing agent was added, and the others were the same as Example 1.

经测试,对比例制得的复合材料颗粒较大、且分布不均匀。该对比例制得复合材料的TEM图如图10所示。After testing, the particles of the composite material prepared in the comparative example were larger and unevenly distributed. The TEM image of the composite material prepared in this comparative example is shown in Figure 10.

前述对本发明的具体示例性实施方案的描述是为了说明和例证的目的。这些描述并非想将本发明限定为所公开的精确形式,并且很显然,根据上述教导,可以进行很多改变和变化。对示例性实施例进行选择和描述的目的在于解释本发明的特定原理及其实际应用,从而使得本领域的技术人员能够实现并利用本发明的各种不同的示例性实施方案以及各种不同的选择和改变。本发明的范围意在由权利要求书及其等同形式所限定。The foregoing descriptions of specific exemplary embodiments of the present invention have been presented for purposes of illustration and illustration. These descriptions are not intended to limit the invention to the precise form disclosed, and obviously many modifications and variations are possible in light of the above teachings. The exemplary embodiments were chosen and described in order to explain certain principles of the invention and its practical application, thereby enabling others skilled in the art to make and utilize various exemplary embodiments of the invention and various different applications. Choice and change. The scope of the invention is intended to be defined by the claims and their equivalents.

Claims (10)

1.一种合成负载型Pt-MXene复合结构催化剂,其特征在于,所述催化剂以MXene为载体,以铂为活性物质,所述铂均匀分散在所述MXene表面,所述铂包括0价铂金属粒子与Pt2+1. A synthetic supported Pt-MXene composite structure catalyst, characterized in that the catalyst uses MXene as a carrier and platinum as an active material. The platinum is evenly dispersed on the surface of the MXene, and the platinum includes zero-valent platinum. Metal particles and Pt 2+ . 2.根据权利要求1所述的合成负载型Pt-MXene复合结构催化剂,其特征在于,所述0价铂金属粒子的粒径为1~5nm;2. The synthetic supported Pt-MXene composite structure catalyst according to claim 1, characterized in that the particle size of the zero-valent platinum metal particles is 1~5nm; 和/或,所述MXene表面的0价铂金属粒子占总Pt含量的70%以上。And/or, the 0-valent platinum metal particles on the surface of the MXene account for more than 70% of the total Pt content. 3.根据权利要求1所述的合成负载型Pt-MXene复合结构催化剂,其特征在于,所述0价铂金属粒子的粒径可达到2nm以下。3. The synthetic supported Pt-MXene composite structure catalyst according to claim 1, characterized in that the particle size of the zero-valent platinum metal particles can reach less than 2 nm. 4.根据权利要求1所述的合成负载型Pt-MXene复合结构催化剂的制备方法,其特征在于,所述制备方法采用乙二醇还原浸渍法,包括:4. The preparation method of synthetic supported Pt-MXene composite structure catalyst according to claim 1, characterized in that the preparation method adopts ethylene glycol reduction impregnation method, including: 步骤S1:将MXene加入到尿素水溶液中,超声混合均匀后,加入氯铂酸,搅拌混合后加热反应,反应后冷却至室温,得到混合溶液;Step S1: Add MXene to the urea aqueous solution, mix evenly with ultrasonic, add chloroplatinic acid, stir and mix, then heat the reaction, cool to room temperature after the reaction, and obtain a mixed solution; 步骤S2:将乙二醇加入到步骤S1得到混合溶液中,混合搅拌后加热,加热结束后继续搅拌,经过后处理后得到合成负载型Pt-MXene复合结构催化剂。Step S2: Add ethylene glycol to the mixed solution obtained in step S1, mix and stir, then heat, continue stirring after heating, and obtain a synthetic supported Pt-MXene composite structure catalyst after post-processing. 5.根据权利要求4所述的制备方法,其特征在于,所述MXene为第IIIB-VIB族金属碳化物。5. The preparation method according to claim 4, characterized in that the MXene is a Group IIIB-VIB metal carbide. 6.根据权利要求4所述的制备方法,其特征在于,所述MXene为Mo2CTx、Ti3C2Tx、V2CTx、Nb2CTx和Cr2CTx中的一种。6. The preparation method according to claim 4, characterized in that the MXene is one of Mo 2 CTx , Ti 3 C 2 Tx, V 2 CTx, Nb 2 CTx and Cr 2 CTx. 7.根据权利要求4所述的制备方法,其特征在于,所述MXene的制备方法包括:将前驱体MAX于刻蚀溶液中超声处理后,发生刻蚀反应,洗涤干燥后,得到MXene。7. The preparation method according to claim 4, characterized in that the preparation method of MXene includes: ultrasonically treating the precursor MAX in an etching solution, causing an etching reaction, and washing and drying to obtain MXene. 8.根据权利要求7所述的制备方法,其特征在于,所述刻蚀溶液为盐酸与氟化铵的混合溶液,所述盐酸的浓度为30~60wt%,所述氟化铵与所述MAX的质量比为1:1;8. The preparation method according to claim 7, characterized in that the etching solution is a mixed solution of hydrochloric acid and ammonium fluoride, the concentration of the hydrochloric acid is 30~60wt%, the ammonium fluoride and the The mass ratio of MAX is 1:1; 和/或,所述超声处理的时间为30~60 min;And/or, the ultrasonic treatment time is 30~60 minutes; 和/或,所述刻蚀反应的温度为140℃~160℃,所述刻蚀反应的时间为12-24 h。And/or, the temperature of the etching reaction is 140°C~160°C, and the time of the etching reaction is 12-24 h. 9.根据权利要求4所述的制备方法,其特征在于,所述步骤S1中尿素水溶液中尿素的质量与水的体积比为(300~400)mg/(200~300)ml;9. The preparation method according to claim 4, characterized in that the volume ratio of the mass of urea in the urea aqueous solution to water in step S1 is (300~400) mg/(200~300) ml; 和/或,所述步骤S1中所述氯铂酸的浓度为0.05M;And/or, the concentration of chloroplatinic acid in step S1 is 0.05M; 和/或,所述步骤S1中搅拌为机械搅拌,机械搅拌的时间为3~4h,或,所述步骤S1中搅拌为超声搅拌,超声搅拌时间为30~60min;And/or, the stirring in step S1 is mechanical stirring, and the mechanical stirring time is 3 to 4 hours; or, the stirring in step S1 is ultrasonic stirring, and the ultrasonic stirring time is 30 to 60 minutes; 和/或,所述步骤S1中加热的温度为90~100℃,加热的时间为1~2h;And/or, the heating temperature in step S1 is 90~100°C, and the heating time is 1~2h; 和/或,所述步骤S2中所述乙二醇与所述混合溶液的体积比为1:1~1:1.5;And/or, the volume ratio of the ethylene glycol and the mixed solution in step S2 is 1:1~1:1.5; 和/或,所述步骤S2中混合搅拌为机械搅拌,机械搅拌的时间为3~4h,或,所述步骤S2中混合搅拌为超声搅拌,超声搅拌时间为30~60min;And/or, the mixing and stirring in step S2 is mechanical stirring, and the mechanical stirring time is 3 to 4 hours; or, the mixing and stirring in step S2 is ultrasonic stirring, and the ultrasonic stirring time is 30 to 60 minutes; 和/或,所述步骤S2中加热的温度为120~130℃,加热时间为1~2h;And/or, the heating temperature in step S2 is 120~130°C, and the heating time is 1~2h; 和/或,所述步骤S2中加热结束后继续搅拌的时间为12~14h。And/or, the time for continuing stirring after heating in step S2 is 12 to 14 hours. 10.一种根据权利要求1-3任一项所述合成负载型Pt-MXene复合结构催化剂或根据权利要求4-9任一项所述制备方法制备得到的合成负载型Pt-MXene复合结构催化剂作为质子交换膜燃料电池氧还原催化剂、水电解析氧催化剂或二氧化碳电还原催化剂的应用。10. A synthetic supported Pt-MXene composite structure catalyst according to any one of claims 1-3 or a synthetic supported Pt-MXene composite structure catalyst prepared according to the preparation method according to any one of claims 4-9 Application as proton exchange membrane fuel cell oxygen reduction catalyst, water electrolysis oxygen catalyst or carbon dioxide electroreduction catalyst.
CN202311237976.6A 2023-09-25 2023-09-25 Composite structure catalyst for synthesizing supported Pt-MXene and preparation method and application thereof Pending CN116995254A (en)

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CN1560946A (en) * 2004-02-23 2005-01-05 北京科技大学 A method for preparing direct methanol fuel cell anode catalyst by stannous acid method
CN102784638A (en) * 2011-05-20 2012-11-21 北京化工大学 New process for preparing Pt-M (Mo, au, ce)/C/TiO2fuel cell anode electrocatalyst by in-situ reduction with illumination
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