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CN111659389A - Platinum-based catalyst containing actinide simple substance or compound - Google Patents

Platinum-based catalyst containing actinide simple substance or compound Download PDF

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CN111659389A
CN111659389A CN202010435578.5A CN202010435578A CN111659389A CN 111659389 A CN111659389 A CN 111659389A CN 202010435578 A CN202010435578 A CN 202010435578A CN 111659389 A CN111659389 A CN 111659389A
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platinum
solution
based catalyst
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王玲钰
欧阳应根
肖松涛
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China Institute of Atomic of Energy
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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
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/89Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with noble metals
    • B01J23/8933Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with noble metals also combined with metals, or metal oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/894Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with noble metals also combined with metals, or metal oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with rare earths or actinides
    • 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
    • B01J23/54Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/56Platinum group metals
    • B01J23/63Platinum group metals with rare earths or actinides
    • 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
    • B01J35/33Electric or magnetic properties
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    • 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
    • H01M4/9041Metals or alloys
    • 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
    • H01M4/921Alloys or mixtures with metallic elements
    • 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
    • H01M4/923Compounds thereof with non-metallic elements
    • 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
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells

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Abstract

The invention belongs to the technical field of catalysts, and relates to a platinum-based catalyst containing an actinide element simple substance or compound. The platinum-based catalyst comprises a catalytic active substance and a catalytic auxiliary substance, wherein the catalytic active substance comprises platinum metal, the catalytic auxiliary substance comprises a cocatalyst, and the cocatalyst comprises one or more of simple substances or compounds of actinide or protactinium. The platinum-based catalyst containing the actinide simple substance or compound has better catalytic performance and stability.

Description

一种含锕系元素单质或化合物的铂基催化剂A platinum-based catalyst containing actinide element or compound

技术领域technical field

本发明属于催化剂技术领域,涉及一种含锕系元素单质或化合物的铂基催化剂。The invention belongs to the technical field of catalysts, and relates to a platinum-based catalyst containing actinide elements or compounds.

背景技术Background technique

催化剂材料与催化技术是当今化学工业发展的基础性、关键性的材料和技术之一。现代工业中,利用催化技术所产生的产值已占国民经济总产值的约30%。Catalyst materials and catalytic technology are one of the basic and key materials and technologies for the development of today's chemical industry. In modern industry, the output value generated by the use of catalytic technology has accounted for about 30% of the total output value of the national economy.

贵金属Pt外层电子排布是5d86s2,其次外层共8个d电子,轨道未被填满。且由于能级中含有未成对电子,故Pt在物理性质中能够表现出较强的铁磁性或顺磁性;而在化学吸附的过程中,Pt的这些d电子能够与被吸附物中的p电子或s电子配对,发生化学吸附,生成中间产物,从而使被吸附的分子活化。The outer electron arrangement of noble metal Pt is 5d 8 6s 2 , followed by 8 d electrons in the outer layer, and the orbitals are not filled. And because the energy level contains unpaired electrons, Pt can show strong ferromagnetism or paramagnetism in physical properties; and in the process of chemical adsorption, these d electrons of Pt can interact with the p electrons in the adsorbate. Or s electron pairing, chemical adsorption occurs, and intermediate products are generated, thereby activating the adsorbed molecules.

现代工业中,铂催化剂主要用于无机化工、石油精炼、有机化工、C1化工、精细化工、汽车尾气和工业气体的净化治理,以及燃料电池与传感器等领域,因而在工业催化、环境保护和绿色能源技术方面有着非常重要的地位,并显示了广阔的应用前景。In modern industry, platinum catalysts are mainly used in the purification and treatment of inorganic chemicals, petroleum refining, organic chemicals, C1 chemicals, fine chemicals, automobile exhaust and industrial gases, as well as fuel cells and sensors. Energy technology has a very important position and shows broad application prospects.

但纯Pt作为催化剂有3个主要的缺点,即利用率低、抗中毒能力低以及价格高昂。针对这些缺点,世界范围内大量的研究致力于开发高活性铂催化剂和降低铂催化剂用量,以提高Pt催化剂的催化活性、选择性,并延长其寿命。However, pure Pt as a catalyst has three main disadvantages, namely, low utilization rate, low anti-poisoning ability and high price. In view of these shortcomings, a large number of researches worldwide are devoted to developing high-activity platinum catalysts and reducing the amount of platinum catalysts to improve the catalytic activity, selectivity, and prolong life of Pt catalysts.

关于Pt催化剂,目前主要的研究方向有:Regarding Pt catalysts, the current main research directions are:

1、一元Pt基催化剂1. One-way Pt-based catalyst

一元Pt基催化剂的研究方向集中在寻找具有优良性能的催化剂载体及改变Pt颗粒的大小、表面状态。例如Zhu等采用功能化多壁碳纳米管分散在聚苯胺中作为载体,合成了Pt/MWCNT/PAN分散性良好的催化剂。研究结果表明,与单纯聚苯胺为载体催化剂相比,该催化剂表现出较高的催化活性。又如Wu等制备了“壳核”结构的纳米碳材料,以炭黑颗粒为“核”负载,以型掺杂的石墨层为“壳”,这种催化剂具有较高的催化活性。又如Zhang等通过无模板电沉积法制备了形貌新颖的纳米花,其形貌具有多孔性,能够提供更大的活性中心。The research direction of one-element Pt-based catalysts focuses on finding catalyst supports with excellent performance and changing the size and surface state of Pt particles. For example, Zhu et al. used functionalized multi-walled carbon nanotubes dispersed in polyaniline as a carrier to synthesize a catalyst with good dispersibility of Pt/MWCNT/PAN. The research results show that the catalyst exhibits higher catalytic activity than pure polyaniline-supported catalyst. Another example is Wu et al. prepared a "shell-core" structure of carbon nanomaterials, with carbon black particles as the "core" load, and the type-doped graphite layer as the "shell", this catalyst has high catalytic activity. Another example is Zhang et al. prepared nanoflowers with novel morphology by template-free electrodeposition method, and their morphology is porous and can provide larger active centers.

2、二元Pt基催化剂2. Binary Pt-based catalyst

在纯Pt催化剂中加入第二种易吸附含氧物质的金属,制备合金型催化剂,将提高催化剂的抗中毒性,进而大大提高催化剂的性能。目前研究较多且催化效果较好的Pt基二元催化剂有PtRu、PtPd、PtSn、PtAu、PtNi、PtCo和金属氧化物(Pt+MOx,其中M=Ti、W、Zr、Ce、Ta)等复合催化剂。Adding a second metal that is easy to adsorb oxygen-containing substances to the pure Pt catalyst to prepare an alloy type catalyst will improve the anti-toxicity of the catalyst, thereby greatly improving the performance of the catalyst. At present, Pt-based binary catalysts with more research and better catalytic effect include PtRu, PtPd, PtSn, PtAu, PtNi, PtCo and metal oxides (Pt+MO x , where M=Ti, W, Zr, Ce, Ta) and other composite catalysts.

3、多元Pt基催化剂3. Multi-component Pt-based catalyst

研究者尝试通过添加第三种甚至第四种金属对Pt基合金改进,从而提高其催化活性。例如Park等研究了Pt/Ni、Pt/Ru/Ni纳米催化剂在甲醇氧化过程中的电子效应与化学效应。又如Jeon等人合成了PtCoCr三元催化剂,其实验结果表明Pt30Co30Cr40对甲醇电氧化性、稳定性及催化效果十分良好,是非常优异的甲醇电氧化催化剂。The researchers tried to improve the Pt-based alloy by adding a third or even a fourth metal, thereby increasing its catalytic activity. For example, Park et al. studied the electronic and chemical effects of Pt/Ni and Pt/Ru/Ni nanocatalysts during methanol oxidation. Another example is Jeon et al. synthesized a PtCoCr ternary catalyst. The experimental results show that Pt 30 Co 30 Cr 40 has very good methanol electro-oxidation, stability and catalytic effect, and is an excellent methanol electro-oxidation catalyst.

综上所述,虽然在贵金属Pt催化领域科学家们已经开展了多项工作,但不同方法各有优劣。且这些Pt催化材料工业化的应用仍面临着很多挑战,比如大规模可控的合成方法、催化材料的稳定性、金属负载量的精确调控、催化剂抗中毒能力,以及如何更好地将金属材料先进的制备方法同碳负载材料有力的结合起来等等。因此,对贵金属Pt催化开发新的思路迫在眉睫。In summary, although scientists have carried out a number of works in the field of noble metal Pt catalysis, different methods have their own advantages and disadvantages. And the industrial application of these Pt catalytic materials still faces many challenges, such as large-scale and controllable synthesis methods, stability of catalytic materials, precise regulation of metal loading, anti-poisoning ability of catalysts, and how to better advance metal materials. The preparation method can be effectively combined with carbon-supported materials and so on. Therefore, it is urgent to develop new ideas for noble metal Pt catalysis.

发明内容SUMMARY OF THE INVENTION

本发明的目的是提供一种含锕系元素单质或化合物的铂基催化剂,以能够具有更好的催化性能与稳定性。The purpose of the present invention is to provide a platinum-based catalyst containing actinide element or compound, so as to have better catalytic performance and stability.

为实现此目的,在基础的实施方案中,本发明提供一种含锕系元素单质或化合物的铂基催化剂,所述的铂基催化剂包含催化活性物质与催化辅助物质,所述的催化活性物质包含金属铂,所述的催化辅助物质包含助催化剂,所述的助催化剂包含锕系元素锕或镤的单质或化合物中的一种或几种(该铂基催化剂可用于燃料电池)。In order to achieve this purpose, in a basic embodiment, the present invention provides a platinum-based catalyst containing an actinide element or compound, the platinum-based catalyst comprises a catalytically active substance and a catalytic auxiliary substance, and the catalytically active substance It contains metal platinum, the catalytic auxiliary material contains a promoter, and the promoter contains one or more of actinide or protactinium element or compound (the platinum-based catalyst can be used in a fuel cell).

在一种优选的实施方案中,本发明提供一种含锕系元素单质或化合物的铂基催化剂,其中所述的催化活性物质与所述的催化辅助物质的质量比为1:0.01-10。In a preferred embodiment, the present invention provides a platinum-based catalyst containing an actinide element or compound, wherein the mass ratio of the catalytically active substance to the catalytic auxiliary substance is 1:0.01-10.

在一种优选的实施方案中,本发明提供一种含锕系元素单质或化合物的铂基催化剂,其中所述的催化活性物质与所述的助催化剂的质量比为1:0.0001-1。In a preferred embodiment, the present invention provides a platinum-based catalyst containing an actinide element or compound, wherein the mass ratio of the catalytically active substance to the promoter is 1:0.0001-1.

在一种优选的实施方案中,本发明提供一种含锕系元素单质或化合物的铂基催化剂,其中所述的助催化剂还包含选自金、银、钴、镍、钯、钌、锡、铋、铜、铁、铱、锰、钼、铑、钨、锌的单质或氧化物中的一种或几种。In a preferred embodiment, the present invention provides a platinum-based catalyst containing an actinide element or compound, wherein the cocatalyst further comprises a catalyst selected from the group consisting of gold, silver, cobalt, nickel, palladium, ruthenium, tin, One or more elements or oxides of bismuth, copper, iron, iridium, manganese, molybdenum, rhodium, tungsten and zinc.

在一种优选的实施方案中,本发明提供一种含锕系元素单质或化合物的铂基催化剂,其中所述的催化辅助物质还包含催化剂载体,选自活性炭、碳化硅、三氧化二铝、石墨烯、二氧化硅、沸石中的一种或几种。In a preferred embodiment, the present invention provides a platinum-based catalyst containing an actinide element or compound, wherein the catalytic auxiliary material further comprises a catalyst carrier selected from the group consisting of activated carbon, silicon carbide, aluminum oxide, One or more of graphene, silica and zeolite.

在一种优选的实施方案中,本发明提供一种含锕系元素单质或化合物的铂基催化剂,其中所述的化合物为无机化合物或有机化合物。In a preferred embodiment, the present invention provides a platinum-based catalyst containing an actinide element or compound, wherein the compound is an inorganic compound or an organic compound.

在一种优选的实施方案中,本发明提供一种含锕系元素单质或化合物的铂基催化剂,其中所述的化合物为氧化物。In a preferred embodiment, the present invention provides a platinum-based catalyst containing an actinide element or compound, wherein the compound is an oxide.

本发明的有益效果在于,本发明的含锕系元素单质或化合物的铂基催化剂具有更好的催化性能与稳定性。The beneficial effect of the present invention is that the platinum-based catalyst containing actinide element or compound of the present invention has better catalytic performance and stability.

具体实施方式Detailed ways

以下通过实施例对本发明的具体实施方式作出进一步的说明。The specific embodiments of the present invention will be further described below through examples.

实施例1:制备实施例Example 1: Preparation Example

取0.6g Vulcan XC-72碳粉,0.1g的Ac2O3粉末,10.25mL的H2PtCl6(0.1mol/L)溶液和17.04mL的NiSO4(0.1mol/L)溶液混合加入到80mL去离子水中,超声30min使其分散均匀,然后在搅拌下,用1mol/L的NaOH溶液调节pH值至8-9后,缓慢加入过量2.0mg/mL的NaBH4溶液,继续搅拌3h。用超纯水洗涤至无Cl-后,于60℃下真空干燥4h,得到Pt-Ni-Ac2O3/C催化剂。Take 0.6g of Vulcan XC-72 carbon powder, 0.1g of Ac 2 O 3 powder, 10.25mL of H 2 PtCl 6 (0.1mol/L) solution and 17.04mL of NiSO 4 (0.1mol/L) solution and add it to 80mL In deionized water, sonicate for 30min to make it disperse uniformly, then adjust the pH to 8-9 with 1mol/L NaOH solution under stirring, slowly add excess 2.0mg/mL NaBH4 solution, and continue stirring for 3h. After washing with ultrapure water until there is no Cl- , vacuum drying at 60 °C for 4 h to obtain a Pt-Ni-Ac 2 O 3 /C catalyst.

实施例2:对照制备实施例Example 2: Comparative Preparation Example

取0.6g Vulcan XC-72碳粉,10.25mL的H2PtCl6(0.1mol/L)溶液和17.04mL的NiSO4(0.1mol/L)溶液混合加入到80mL去离子水中,超声30min使其分散均匀,然后在搅拌下,用1mol/L的NaOH溶液调节pH值至8-9后,缓慢加入过量2.0mg/mL的NaBH4溶液,继续搅拌3h。用超纯水洗涤至无Cl-后,于60℃下真空干燥4h,得到Pt-Ni/C催化剂。Mix 0.6g Vulcan XC-72 carbon powder, 10.25mL H 2 PtCl 6 (0.1mol/L) solution and 17.04mL NiSO 4 (0.1mol/L) solution into 80mL deionized water, ultrasonicate for 30min to disperse After the pH value was adjusted to 8-9 with 1 mol/L NaOH solution under stirring, an excess of 2.0 mg/mL NaBH 4 solution was slowly added, and stirring was continued for 3 h. After washing with ultrapure water to no Cl- , vacuum drying at 60 °C for 4 h to obtain a Pt-Ni/C catalyst.

实施例3:制备实施例Example 3: Preparation Example

取0.6g Vulcan XC-72碳粉,0.1g Ac2O3粉末,与80mL乙二醇加入250mL烧杯中,超声振荡2h,滴加10.25mL的H2PtCl6(0.1mol/L)溶液和16.97mL的CoCl2(0.1mol/L)溶液,再加入21mL甲酸,室温搅拌30min,放入微波炉中加热20s停10s反复5次,然后加热10s停10s反复5次,冷却抽滤,真空烘干,得到Pt-Co-Ac2O3/C催化剂。Take 0.6g of Vulcan XC-72 carbon powder, 0.1g of Ac 2 O 3 powder, and 80mL of ethylene glycol into a 250mL beaker, ultrasonically shake for 2h, dropwise add 10.25mL of H 2 PtCl 6 (0.1mol/L) solution and 16.97 mL of CoCl 2 (0.1 mol/L) solution, add 21 mL of formic acid, stir at room temperature for 30 min, put it in a microwave oven to heat for 20 s, stop for 10 s and repeat 5 times, then heat for 10 s and stop for 10 s and repeat 5 times, cool and suction filter, vacuum dry, A Pt-Co-Ac 2 O 3 /C catalyst was obtained.

实施例4:对照制备实施例Example 4: Comparative Preparation Example

取0.6g Vulcan XC-72碳粉,与80mL乙二醇加入250mL烧杯中,超声振荡2h,滴加10.25mL的H2PtCl6(0.1mol/L)溶液和16.97mL的CoCl2(0.1mol/L)溶液,再加入21mL甲酸,室温搅拌30min,放入微波炉中加热20s停10s反复5次,然后加热10s停10s反复5次,冷却抽滤,真空烘干,得到Pt-Co/C催化剂。Take 0.6g of Vulcan XC-72 carbon powder, add 80mL of ethylene glycol into a 250mL beaker, ultrasonically shake for 2h, dropwise add 10.25mL of H 2 PtCl 6 (0.1mol/L) solution and 16.97mL of CoCl 2 (0.1mol/L) L) solution, then add 21 mL of formic acid, stir at room temperature for 30 min, put it into a microwave oven and heat for 20 s, stop for 10 s and repeat 5 times, then heat for 10 s and stop for 10 s and repeat 5 times, cool and suction filter, and vacuum dry to obtain a Pt-Co/C catalyst.

实施例5:制备实施例Example 5: Preparation Example

取0.6g Vulcan XC-72碳粉与0.1g Ac2O3粉末加入到HCOOH含量为0.7mol的水溶液中,超声30min后,将所得的悬浊液加热至80℃,在不断搅拌下,将10.25mL的H2PtCl6(0.1mol/L)溶液和9.4mL的PdCl2(0.1mol/L)溶液滴加到悬浊液中。继续在80℃搅拌2h,以保证Pd和Pt完全被还原。冷却后,用超纯水抽滤洗涤多次,直至无Cl-为止。最后,将所得催化剂放在60℃烘箱中真空干燥,得到Pt-Pd-Ac2O3/C催化剂。Take 0.6 g of Vulcan XC-72 carbon powder and 0.1 g of Ac 2 O 3 powder and add it to an aqueous solution with a HCOOH content of 0.7 mol. After sonicating for 30 min, the obtained suspension was heated to 80 ° C, and under constant stirring, 10.25 mL of H 2 PtCl 6 (0.1 mol/L) solution and 9.4 mL of PdCl 2 (0.1 mol/L) solution were added dropwise to the suspension. Continue stirring at 80 °C for 2 h to ensure complete reduction of Pd and Pt. After cooling, it was washed several times with ultrapure water suction filtration until there was no Cl- . Finally, the obtained catalyst was vacuum-dried in an oven at 60°C to obtain a Pt-Pd-Ac 2 O 3 /C catalyst.

实施例6:对照制备实施例Example 6: Comparative Preparation Example

取0.6g Vulcan XC-72碳粉加入到HCOOH含量为0.7mol的水溶液中,超声30min后,将所得的悬浊液加热至80℃,在不断搅拌下,将10.25mL的H2PtCl6(0.1mol/L)溶液和9.4mL的PdCl2(0.1mol/L)溶液滴加到悬浊液中。继续在80℃搅拌2h,以保证Pd和Pt完全被还原。冷却后,用超纯水抽滤洗涤多次,直至无Cl-为止。最后,将所得催化剂放在60℃烘箱中真空干燥,得到Pt-Pd/C催化剂。Take 0.6 g of Vulcan XC-72 carbon powder and add it to an aqueous solution with a HCOOH content of 0.7 mol. After ultrasonication for 30 min, the obtained suspension was heated to 80° C. Under constant stirring, 10.25 mL of H 2 PtCl 6 (0.1 mol/L) solution and 9.4 mL of PdCl 2 (0.1 mol/L) solution were added dropwise to the suspension. Continue stirring at 80 °C for 2 h to ensure complete reduction of Pd and Pt. After cooling, it was washed several times with ultrapure water suction filtration until there was no Cl- . Finally, the obtained catalyst was vacuum-dried in an oven at 60 °C to obtain a Pt-Pd/C catalyst.

实施例7:制备实施例Example 7: Preparation Example

取0.6g Vulcan XC-72活性炭,0.1g Ac2O3粉末,10.25mL的H2PtCl6(0.1mol/L)溶液、5.08mL的HAuCl4(0.1mol/L)溶液和17.04mL的NiSO4(0.1mol/L)溶液混合加入到80mL超纯水中,将所得的悬浊液超声1h。再加入200mL乙二醇(EG)溶液,超声1h后,将所得溶液在水浴加热到90℃,并不断搅拌4h。冷却至室温过滤后,将所得催化剂用蒸馏水和乙醇混合溶液清洗几次,60℃真空干燥,得到Pt-Au-Ni-Ac2O3/C催化剂。Take 0.6g Vulcan XC-72 activated carbon, 0.1g Ac 2 O 3 powder, 10.25mL of H 2 PtCl 6 (0.1mol/L) solution, 5.08mL of HAuCl 4 (0.1mol/L) solution and 17.04mL of NiSO 4 (0.1 mol/L) solution was mixed and added to 80 mL of ultrapure water, and the obtained suspension was sonicated for 1 h. Then 200 mL of ethylene glycol (EG) solution was added, and after sonication for 1 h, the resulting solution was heated to 90° C. in a water bath and stirred continuously for 4 h. After cooling to room temperature and filtering, the obtained catalyst was washed several times with a mixed solution of distilled water and ethanol, and vacuum dried at 60°C to obtain a Pt-Au-Ni-Ac 2 O 3 /C catalyst.

实施例8:对照制备实施例Example 8: Comparative Preparation Example

取0.6g Vulcan XC-72活性炭,10.25mL的H2PtCl6(0.1mol/L)溶液、5.08mL的HAuCl4(0.1mol/L)溶液和17.04mL的NiSO4(0.1mol/L)溶液混合加入到80mL超纯水中,将所得的悬浊液超声1h。再加入200mL乙二醇(EG)溶液,超声1h后,将所得溶液在水浴加热到90℃,并不断搅拌4h。冷却至室温过滤后,将所得催化剂用蒸馏水和乙醇混合溶液清洗几次,60℃真空干燥,得到Pt-Au-Ni/C催化剂。Mix 0.6g Vulcan XC-72 activated carbon, 10.25mL H 2 PtCl 6 (0.1mol/L) solution, 5.08mL HAuCl 4 (0.1mol/L) solution and 17.04mL NiSO 4 (0.1mol/L) solution It was added to 80 mL of ultrapure water, and the resulting suspension was sonicated for 1 h. Then 200 mL of ethylene glycol (EG) solution was added, and after sonication for 1 h, the resulting solution was heated to 90° C. in a water bath and stirred continuously for 4 h. After cooling to room temperature and filtering, the obtained catalyst was washed several times with a mixed solution of distilled water and ethanol, and vacuum-dried at 60°C to obtain a Pt-Au-Ni/C catalyst.

实施例9:制备实施例Example 9: Preparation Example

取0.6g的棕黄色氧化石墨烯,0.1g Ac2O3粉末加入到50mL去离子水中,超声分散30min,用移液枪移取10.25mL的H2PtCl6(0.1mol/L)溶液、17.04mL的NiSO4(0.1mol/L)溶液和15.74mL的CuCl2(0.1mol/L)溶液混合加入到氧化石墨烯溶液中,搅拌10min后移入双口烧瓶中,加入9.5mL去离子水,在0℃,N2气气氛下混合均匀后,用注射器快速注入5mL7.72mmol/L的KBH4溶液,溶液颜色由棕黄色变为黑色,继续在0℃,N2气气氛下搅拌30min使其充分反应,最后抽滤洗涤,烘干研磨,得到Pt-Ni-Cu-Ac2O3/C催化剂。Take 0.6g of brownish yellow graphene oxide, add 0.1g of Ac 2 O 3 powder to 50mL of deionized water, disperse it ultrasonically for 30min, and use a pipette to remove 10.25mL of H 2 PtCl 6 (0.1mol/L) solution, 17.04 mL of NiSO 4 (0.1 mol/L) solution and 15.74 mL of CuCl 2 (0.1 mol/L) solution were mixed into the graphene oxide solution, stirred for 10 min, and then transferred to a two-necked flask, and 9.5 mL of deionized water was added. After mixing uniformly at 0°C under N2 gas atmosphere, 5 mL of 7.72 mmol/L KBH4 solution was rapidly injected with a syringe, and the color of the solution changed from brown to black. Continue to stir at 0°C under N2 gas atmosphere for 30 min to make it fully reaction, finally suction filtration washing, drying and grinding to obtain a Pt-Ni-Cu-Ac 2 O 3 /C catalyst.

实施例10:对照制备实施例Example 10: Comparative Preparation Example

取0.6g的棕黄色氧化石墨烯加入到50mL去离子水中,超声分散30min,用移液枪移取10.25mL的H2PtCl6(0.1mol/L)溶液、17.04mL的NiSO4(0.1mol/L)溶液和15.74mL的CuCl2(0.1mol/L)溶液混合加入到氧化石墨烯溶液中,搅拌10min后移入双口烧瓶中,加入9.5mL去离子水,在0℃,N2气气氛下混合均匀后,用注射器快速注入5mL 7.72mmol/L的KBH4溶液,溶液颜色由棕黄色变为黑色,继续在0℃,N2气气氛下搅拌30min使其充分反应,最后抽滤洗涤,烘干研磨,得到Pt-Ni-Cu/C催化剂。Take 0.6g of brown-yellow graphene oxide and add it to 50mL of deionized water, ultrasonically disperse for 30min, and use a pipette to pipette 10.25mL of H 2 PtCl 6 (0.1mol/L) solution, 17.04mL of NiSO 4 (0.1mol/L) solution L) solution and 15.74mL of CuCl 2 (0.1mol/L) solution were mixed into the graphene oxide solution, stirred for 10min and then transferred to a two-necked flask, 9.5mL of deionized water was added, at 0°C, under N2 gas atmosphere After mixing evenly, quickly inject 5mL of 7.72mmol/L KBH4 solution with a syringe, the color of the solution changes from brown to black, continue to stir at 0 °C for 30min under N2 gas atmosphere to make it fully react, and finally filter and wash, bake. Dry grinding to obtain a Pt-Ni-Cu/C catalyst.

实施例11:制备实施例Example 11: Preparation Example

取0.6g Vulcan XC-72活性炭,0.1g Ac2O3粉末,加入超纯水与异丙醇(体积比2:1)的混合溶液中,超声分散0.5h。再依次滴加10.25mL的H2PtCl6(0.1mol/L)溶液、9.4mL的PdCl2(0.1mol/L)溶液和15.74mL的CuCl2(0.1mol/L)溶液和20mg柠檬酸钠,搅拌1h。调节溶液PH>12,升温至80℃,缓慢滴加0.2mol/L过量的硼氢化钠溶液,保持2h。随后室温下继续搅拌3h,抽滤洗涤,60℃鼓风烘干,得到Pt-Pd-Cu-Ac2O3/C催化剂。Take 0.6g of Vulcan XC-72 activated carbon and 0.1g of Ac 2 O 3 powder, add it into a mixed solution of ultrapure water and isopropanol (volume ratio 2:1), and ultrasonically disperse for 0.5h. Then 10.25mL of H 2 PtCl 6 (0.1mol/L) solution, 9.4mL of PdCl 2 (0.1mol/L) solution, 15.74mL of CuCl 2 (0.1mol/L) solution and 20mg of sodium citrate were added dropwise in sequence, Stir for 1 h. The pH of the solution was adjusted to >12, the temperature was raised to 80 °C, and an excess of 0.2 mol/L sodium borohydride solution was slowly added dropwise for 2 h. Subsequently, stirring was continued at room temperature for 3 hours, and the mixture was washed with suction, and dried by blowing at 60° C. to obtain a Pt-Pd-Cu-Ac 2 O 3 /C catalyst.

实施例12:对照制备实施例Example 12: Comparative Preparation Example

取0.6g Vulcan XC-72活性炭,加入超纯水与异丙醇(体积比2:1)的混合溶液中,超声分散0.5h。再依次滴加10.25mL的H2PtCl6(0.1mol/L)溶液、9.4mL的PdCl2(0.1mol/L)溶液和15.74mL的CuCl2(0.1mol/L)溶液和20mg柠檬酸钠,搅拌1h。调节溶液PH>12,升温至80℃,缓慢滴加0.2mol/L过量的硼氢化钠溶液,保持2h。随后室温下继续搅拌3h,抽滤洗涤,60℃鼓风烘干,得到Pt-Pd-Cu/C催化剂。Take 0.6g of Vulcan XC-72 activated carbon, add it to a mixed solution of ultrapure water and isopropanol (volume ratio 2:1), and disperse it ultrasonically for 0.5h. Then 10.25mL of H 2 PtCl 6 (0.1mol/L) solution, 9.4mL of PdCl 2 (0.1mol/L) solution, 15.74mL of CuCl 2 (0.1mol/L) solution and 20mg of sodium citrate were added dropwise in sequence, Stir for 1 h. The pH of the solution was adjusted to >12, the temperature was raised to 80 °C, and an excess of 0.2 mol/L sodium borohydride solution was slowly added dropwise for 2 h. Subsequently, stirring was continued for 3 h at room temperature, suction filtration and washing, and air drying at 60 °C was performed to obtain a Pt-Pd-Cu/C catalyst.

实施例13:制备实施例Example 13: Preparation Example

取0.6g Vulcan XC-72碳粉,0.1g的PaO2粉末,10.25mL的H2PtCl6(0.1mol/L)溶液和17.04mL的NiSO4(0.1mol/L)溶液混合加入到80mL去离子水中,超声30min使其分散均匀,然后在搅拌下,用1mol/L的NaOH溶液调节pH值至8-9后,缓慢加入过量2.0mg/mL的NaBH4溶液,继续搅拌3h。用超纯水洗涤至无Cl-后,于60℃下真空干燥4h,得到Pt-Ni-PaO2/C催化剂。Take 0.6g Vulcan XC-72 carbon powder, 0.1g PaO 2 powder, 10.25mL H 2 PtCl 6 (0.1mol/L) solution and 17.04mL NiSO 4 (0.1mol/L) solution and add it to 80mL deionized In water, ultrasonicate for 30min to make it dispersed evenly, then adjust the pH to 8-9 with 1mol/L NaOH solution under stirring, slowly add excess 2.0mg/mL NaBH4 solution, and continue stirring for 3h. After washing with ultrapure water until Cl - free, vacuum drying at 60 ℃ for 4 h to obtain Pt-Ni-PaO 2 /C catalyst.

实施例14:制备实施例Example 14: Preparation Example

取0.6g Vulcan XC-72碳粉,0.1g PaO2粉末,与80mL乙二醇加入250mL烧杯中,超声振荡2h,滴加10.25mL的H2PtCl6(0.1mol/L)溶液和16.97mL的CoCl2(0.1mol/L)溶液,再加入21mL甲酸,室温搅拌30min,放入微波炉中加热20s停10s反复5次,然后加热10s停10s反复5次,冷却抽滤,真空烘干,得到Pt-Co-PaO2/C催化剂。Take 0.6g Vulcan XC-72 carbon powder, 0.1g PaO 2 powder, and 80mL ethylene glycol into a 250mL beaker, ultrasonically shake for 2h, dropwise add 10.25mL H 2 PtCl 6 (0.1mol/L) solution and 16.97mL CoCl 2 (0.1mol/L) solution, then add 21mL of formic acid, stir at room temperature for 30min, put it in a microwave oven to heat for 20s, stop for 10s and repeat 5 times, then heat for 10s and stop for 10s and repeat 5 times, cool and suction filter, and vacuum dry to obtain Pt -Co-PaO 2 /C catalyst.

实施例15:制备实施例Example 15: Preparation Example

取0.6g Vulcan XC-72碳粉与0.1g PaO2粉末加入到HCOOH含量为0.7mol的水溶液中,超声30min后,将所得的悬浊液加热至80℃,在不断搅拌下,将10.25mL的H2PtCl6(0.1mol/L)溶液和9.4mL的PdCl2(0.1mol/L)溶液滴加到悬浊液中。继续在80℃搅拌2h,以保证Pd和Pt完全被还原。冷却后,用超纯水抽滤洗涤多次,直至无Cl-为止。最后,将所得催化剂放在60℃烘箱中真空干燥,得到Pt-Pd-PaO2/C催化剂。Take 0.6 g of Vulcan XC-72 carbon powder and 0.1 g of PaO 2 powder and add it to an aqueous solution with a HCOOH content of 0.7 mol. After sonicating for 30 min, the resulting suspension was heated to 80 °C, and under constant stirring, 10.25 mL of H 2 PtCl 6 (0.1 mol/L) solution and 9.4 mL of PdCl 2 (0.1 mol/L) solution were added dropwise to the suspension. Continue stirring at 80 °C for 2 h to ensure complete reduction of Pd and Pt. After cooling, it was washed several times with ultrapure water suction filtration until there was no Cl- . Finally, the obtained catalyst was vacuum-dried in an oven at 60 °C to obtain a Pt-Pd-PaO 2 /C catalyst.

实施例16:制备实施例Example 16: Preparation Example

取0.6g Vulcan XC-72活性炭,0.1g PaO2粉末,10.25mL的H2PtCl6(0.1mol/L)溶液、5.08mL的HAuCl4(0.1mol/L)溶液和17.04mL的NiSO4(0.1mol/L)溶液混合加入到80mL超纯水中,将所得的悬浊液超声1h。再加入200mL乙二醇(EG)溶液,超声1h后,将所得溶液在水浴加热到90℃,并不断搅拌4h。冷却至室温过滤后,将所得催化剂用蒸馏水和乙醇混合溶液清洗几次,60℃真空干燥,得到Pt-Au-Ni-PaO2/C催化剂。Take 0.6g Vulcan XC-72 activated carbon, 0.1g PaO 2 powder, 10.25mL of H 2 PtCl 6 (0.1mol/L) solution, 5.08mL of HAuCl 4 (0.1mol/L) solution and 17.04mL of NiSO 4 (0.1 mol/L) solution was mixed into 80 mL of ultrapure water, and the resulting suspension was sonicated for 1 h. Then 200 mL of ethylene glycol (EG) solution was added, and after sonication for 1 h, the resulting solution was heated to 90° C. in a water bath and stirred continuously for 4 h. After cooling to room temperature and filtering, the obtained catalyst was washed several times with a mixed solution of distilled water and ethanol, and dried in vacuum at 60°C to obtain a Pt-Au-Ni-PaO 2 /C catalyst.

实施例17:制备实施例Example 17: Preparation Example

取0.6g的棕黄色氧化石墨烯,0.1g PaO2粉末加入到50mL去离子水中,超声分散30min,用移液枪移取10.25mL的H2PtCl6(0.1mol/L)溶液、17.04mL的NiSO4(0.1mol/L)溶液和15.74mL的CuCl2(0.1mol/L)溶液混合加入到氧化石墨烯溶液中,搅拌10min后移入双口烧瓶中,加入9.5mL去离子水,在0℃,N2气气氛下混合均匀后,用注射器快速注入5mL7.72mmol/L的KBH4溶液,溶液颜色由棕黄色变为黑色,继续在0℃,N2气气氛下搅拌30min使其充分反应,最后抽滤洗涤,烘干研磨,得到Pt-Ni-Cu-PaO2/C催化剂。Take 0.6g of brown-yellow graphene oxide, add 0.1g PaO 2 powder to 50mL of deionized water, ultrasonically disperse for 30min, use a pipette to remove 10.25mL of H 2 PtCl 6 (0.1mol/L) solution, 17.04mL of NiSO 4 (0.1 mol/L) solution and 15.74 mL of CuCl 2 (0.1 mol/L) solution were mixed into the graphene oxide solution, stirred for 10 min, and then transferred to a two-necked flask. , After mixing evenly under N2 gas atmosphere, quickly inject 5mL 7.72mmol/L KBH4 solution with a syringe, the color of the solution changes from brown to black, continue to stir at 0 °C under N2 gas atmosphere for 30min to make it fully react, Finally, suction filtration washing, drying and grinding to obtain a Pt-Ni-Cu-PaO 2 /C catalyst.

实施例18:制备实施例Example 18: Preparation Example

取0.6g Vulcan XC-72活性炭,0.1g PaO2粉末,加入超纯水与异丙醇(体积比2:1)的混合溶液中,超声分散0.5h。再依次滴加10.25mL的H2PtCl6(0.1mol/L)溶液、9.4mL的PdCl2(0.1mol/L)溶液和15.74mL的CuCl2(0.1mol/L)溶液和20mg柠檬酸钠,搅拌1h。调节溶液PH>12,升温至80℃,缓慢滴加0.2mol/L过量的硼氢化钠溶液,保持2h。随后室温下继续搅拌3h,抽滤洗涤,60℃鼓风烘干,得到Pt-Pd-Cu-PaO2/C催化剂。Take 0.6g of Vulcan XC-72 activated carbon and 0.1g of PaO 2 powder, add it to the mixed solution of ultrapure water and isopropanol (volume ratio 2:1), and disperse by ultrasonic for 0.5h. Then 10.25mL of H 2 PtCl 6 (0.1mol/L) solution, 9.4mL of PdCl 2 (0.1mol/L) solution, 15.74mL of CuCl 2 (0.1mol/L) solution and 20mg of sodium citrate were added dropwise in sequence, Stir for 1 h. The pH of the solution was adjusted to >12, the temperature was raised to 80 °C, and an excess of 0.2 mol/L sodium borohydride solution was slowly added dropwise for 2 h. Subsequently, stirring was continued at room temperature for 3 hours, suction filtration and washing, and air drying at 60° C. to obtain a Pt-Pd-Cu-PaO 2 /C catalyst.

实施例19:稳定性测试实施例Example 19: Stability Test Example

分别测定实施例1-18获得的催化剂的稳定性,具体方法为:使用电化学工作站三电极体系测试催化剂的I-t曲线,并依此判断催化剂稳定性,其中滴涂催化剂的玻碳电极做工作电极,饱和甘汞电极做参比电极,铂丝电极做对电极。待测溶液为0.5mol/L C2H5OH+0.5mol/L H2SO4,测试之前向溶液中通15分钟高纯氮气,以排除氧气干扰。所有催化剂的测试电位统一为0.6V,测试时间为1000s。结果如下表1所示。The stability of the catalysts obtained in Examples 1-18 was measured respectively, and the specific method was as follows: using the electrochemical workstation three-electrode system to test the It curve of the catalyst, and judge the stability of the catalyst accordingly, wherein the glassy carbon electrode on which the catalyst was dripped was used as the working electrode. , saturated calomel electrode as the reference electrode, platinum wire electrode as the counter electrode. The solution to be tested is 0.5mol/LC 2 H 5 OH+0.5mol/LH 2 SO 4 , and high-purity nitrogen gas was passed into the solution for 15 minutes before the test to eliminate the interference of oxygen. The test potential of all catalysts was uniformly 0.6 V, and the test time was 1000 s. The results are shown in Table 1 below.

表1催化剂稳定性测试结果Table 1 Catalyst stability test results

Figure BDA0002502132410000081
Figure BDA0002502132410000081

Figure BDA0002502132410000091
Figure BDA0002502132410000091

显然,本领域的技术人员可以对本发明进行各种改动和变型而不脱离本发明的精神和范围。这样,倘若对本发明的这些修改和变型属于本发明权利要求及其同等技术的范围之内,则本发明也意图包含这些改动和变型在内。上述实施例或实施方式只是对本发明的举例说明,本发明也可以以其它的特定方式或其它的特定形式实施,而不偏离本发明的要旨或本质特征。因此,描述的实施方式从任何方面来看均应视为说明性而非限定性的。本发明的范围应由附加的权利要求说明,任何与权利要求的意图和范围等效的变化也应包含在本发明的范围内。It will be apparent to those skilled in the art that various modifications and variations can be made in the present invention without departing from the spirit and scope of the invention. Thus, provided that these modifications and variations of the present invention fall within the scope of the claims of the present invention and their technical equivalents, the present invention is also intended to include such modifications and variations. The above-mentioned embodiments or implementations are merely illustrative of the present invention, and the present invention may also be implemented in other specific forms or other specific forms without departing from the gist or essential characteristics of the present invention. Accordingly, the described embodiments are to be regarded in all respects as illustrative and not restrictive. The scope of the present invention should be indicated by the appended claims, and any changes equivalent to the intent and scope of the claims should also be included within the scope of the present invention.

Claims (7)

1. A platinum-based catalyst comprising an actinide element or compound, characterized in that: the platinum-based catalyst comprises a catalytic active substance and a catalytic auxiliary substance, wherein the catalytic active substance comprises platinum metal, the catalytic auxiliary substance comprises a cocatalyst, and the cocatalyst comprises one or more of simple substances or compounds of actinide or protactinium.
2. The platinum-based catalyst according to claim 1, characterized in that: the mass ratio of the catalytic active substance to the catalytic auxiliary substance is 1: 0.01-10.
3. The platinum-based catalyst according to claim 1, characterized in that: the mass ratio of the catalytic active substance to the cocatalyst is 1: 0.0001-1.
4. The platinum-based catalyst according to claim 1, characterized in that: the catalyst promoter also comprises one or more of simple substances or oxides of gold, silver, cobalt, nickel, palladium, ruthenium, tin, bismuth, copper, iron, iridium, manganese, molybdenum, rhodium, tungsten and zinc.
5. The platinum-based catalyst according to claim 1, characterized in that: the catalytic auxiliary substance also comprises a catalyst carrier which is selected from one or more of active carbon, silicon carbide, aluminum oxide, graphene, silicon dioxide and zeolite.
6. The platinum-based catalyst according to claim 1, characterized in that: the compound is an inorganic compound or an organic compound.
7. The platinum-based catalyst according to claim 1, characterized in that: the compound is an oxide.
CN202010435578.5A 2020-05-21 2020-05-21 Platinum-based catalyst containing actinide simple substance or compound Pending CN111659389A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN116809052A (en) * 2023-08-29 2023-09-29 北京大学 An actinide ion-graphdiyne composite material and its preparation method and application

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN116809052A (en) * 2023-08-29 2023-09-29 北京大学 An actinide ion-graphdiyne composite material and its preparation method and application
CN116809052B (en) * 2023-08-29 2023-11-28 北京大学 An actinide ion-graphdiyne composite material and its preparation method and application

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