CN114725409B - Platinum-nickel nanocrystalline modified carbon-based catalyst, gram-grade low-pressure preparation method and application thereof - Google Patents
Platinum-nickel nanocrystalline modified carbon-based catalyst, gram-grade low-pressure preparation method and application thereof Download PDFInfo
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- 239000003054 catalyst Substances 0.000 title abstract description 85
- PCLURTMBFDTLSK-UHFFFAOYSA-N nickel platinum Chemical compound [Ni].[Pt] PCLURTMBFDTLSK-UHFFFAOYSA-N 0.000 title abstract description 44
- 150000001721 carbon Chemical class 0.000 title abstract description 29
- 238000002360 preparation method Methods 0.000 title abstract description 22
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 abstract description 72
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 36
- 229910052760 oxygen Inorganic materials 0.000 abstract description 36
- 239000001301 oxygen Substances 0.000 abstract description 36
- 239000002159 nanocrystal Substances 0.000 abstract description 35
- 238000006722 reduction reaction Methods 0.000 abstract description 34
- 229910052697 platinum Inorganic materials 0.000 abstract description 29
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 abstract description 25
- 239000002243 precursor Substances 0.000 abstract description 18
- 239000006229 carbon black Substances 0.000 abstract description 17
- 239000002904 solvent Substances 0.000 abstract description 11
- 239000003381 stabilizer Substances 0.000 abstract description 11
- 238000006243 chemical reaction Methods 0.000 abstract description 10
- 239000003795 chemical substances by application Substances 0.000 abstract description 10
- 229910052759 nickel Inorganic materials 0.000 abstract description 9
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 230000009467 reduction Effects 0.000 abstract description 3
- 229910002844 PtNi Inorganic materials 0.000 description 56
- 239000000243 solution Substances 0.000 description 34
- WPYMKLBDIGXBTP-UHFFFAOYSA-N benzoic acid Chemical compound OC(=O)C1=CC=CC=C1 WPYMKLBDIGXBTP-UHFFFAOYSA-N 0.000 description 30
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 26
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 26
- LZZYPRNAOMGNLH-UHFFFAOYSA-M Cetrimonium bromide Chemical compound [Br-].CCCCCCCCCCCCCCCC[N+](C)(C)C LZZYPRNAOMGNLH-UHFFFAOYSA-M 0.000 description 16
- -1 platinum-nickel nanocrystal-modified carbon Chemical class 0.000 description 16
- 239000005711 Benzoic acid Substances 0.000 description 15
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- 235000010233 benzoic acid Nutrition 0.000 description 15
- 230000000052 comparative effect Effects 0.000 description 14
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- 238000001035 drying Methods 0.000 description 13
- SHWZFQPXYGHRKT-FDGPNNRMSA-N (z)-4-hydroxypent-3-en-2-one;nickel Chemical compound [Ni].C\C(O)=C\C(C)=O.C\C(O)=C\C(C)=O SHWZFQPXYGHRKT-FDGPNNRMSA-N 0.000 description 12
- KLFRPGNCEJNEKU-FDGPNNRMSA-L (z)-4-oxopent-2-en-2-olate;platinum(2+) Chemical compound [Pt+2].C\C([O-])=C\C(C)=O.C\C([O-])=C\C(C)=O KLFRPGNCEJNEKU-FDGPNNRMSA-L 0.000 description 12
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 12
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- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 9
- 229910052799 carbon Inorganic materials 0.000 description 9
- 238000003917 TEM image Methods 0.000 description 8
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- 229910002462 C-Pt Inorganic materials 0.000 description 7
- 238000011056 performance test Methods 0.000 description 7
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- 229910052739 hydrogen Inorganic materials 0.000 description 4
- 239000001257 hydrogen Substances 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 3
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- VLTRZXGMWDSKGL-UHFFFAOYSA-N perchloric acid Chemical compound OCl(=O)(=O)=O VLTRZXGMWDSKGL-UHFFFAOYSA-N 0.000 description 2
- 238000001878 scanning electron micrograph Methods 0.000 description 2
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- 101001121408 Homo sapiens L-amino-acid oxidase Proteins 0.000 description 1
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- 102100026388 L-amino-acid oxidase Human genes 0.000 description 1
- 229910021586 Nickel(II) chloride Inorganic materials 0.000 description 1
- 102100023591 Polyphosphoinositide phosphatase Human genes 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 101100012902 Saccharomyces cerevisiae (strain ATCC 204508 / S288c) FIG2 gene Proteins 0.000 description 1
- 101100233916 Saccharomyces cerevisiae (strain ATCC 204508 / S288c) KAR5 gene Proteins 0.000 description 1
- 239000006230 acetylene black Substances 0.000 description 1
- 239000003929 acidic solution Substances 0.000 description 1
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- 230000005611 electricity Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000010493 gram-scale synthesis Methods 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 239000003273 ketjen black Substances 0.000 description 1
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- 239000002184 metal Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- QMMRZOWCJAIUJA-UHFFFAOYSA-L nickel dichloride Chemical compound Cl[Ni]Cl QMMRZOWCJAIUJA-UHFFFAOYSA-L 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000037361 pathway Effects 0.000 description 1
- WVDDGKGOMKODPV-ZQBYOMGUSA-N phenyl(114C)methanol Chemical compound O[14CH2]C1=CC=CC=C1 WVDDGKGOMKODPV-ZQBYOMGUSA-N 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 238000011112 process operation Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
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- 230000027756 respiratory electron transport chain Effects 0.000 description 1
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/90—Selection of catalytic material
- H01M4/92—Metals of platinum group
- H01M4/921—Alloys or mixtures with metallic elements
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/90—Selection of catalytic material
- H01M4/92—Metals of platinum group
- H01M4/925—Metals of platinum group supported on carriers, e.g. powder carriers
- H01M4/926—Metals of platinum group supported on carriers, e.g. powder carriers on carbon or graphite
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- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/10—Fuel cells with solid electrolytes
- H01M8/1016—Fuel cells with solid electrolytes characterised by the electrolyte material
- H01M8/1018—Polymeric electrolyte materials
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/10—Fuel cells with solid electrolytes
- H01M2008/1095—Fuel cells with polymeric electrolytes
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
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Abstract
本发明公开了一种铂镍纳米晶修饰碳基催化剂及其克级低压制备方法与应用。所述克级低压制备方法包括:使包含铂前驱体、镍前驱体、炭黑、稳定剂、结构导向剂和溶剂的混合反应体系于130~210℃常压反应12h,制得铂镍纳米晶修饰碳基催化剂。本发明制备的铂镍纳米晶修饰碳基催化剂的氧还原反应性能显著提升,同时铂镍纳米晶修饰碳基催化剂可在常压下合成,具有铂含量低、氧还原性能优异、稳定性高、且可克级生产制备等优点,可大幅度降低生产成本,具有十分广泛的工业化应用前景。
The present invention discloses a platinum-nickel nanocrystal modified carbon-based catalyst and a gram-level low-pressure preparation method and application thereof. The gram-level low-pressure preparation method comprises: reacting a mixed reaction system comprising a platinum precursor, a nickel precursor, carbon black, a stabilizer, a structure directing agent and a solvent at 130-210° C. under normal pressure for 12 hours to obtain a platinum-nickel nanocrystal modified carbon-based catalyst. The oxygen reduction reaction performance of the platinum-nickel nanocrystal modified carbon-based catalyst prepared by the present invention is significantly improved. At the same time, the platinum-nickel nanocrystal modified carbon-based catalyst can be synthesized under normal pressure, has the advantages of low platinum content, excellent oxygen reduction performance, high stability, and can be produced and prepared at the gram level, which can greatly reduce the production cost and has a very broad prospect for industrial application.
Description
技术领域Technical Field
本发明属于材料和能源催化技术领域,具体涉及一种铂镍纳米晶修饰碳基催化剂及其克级低压制备方法与应用。The invention belongs to the technical field of material and energy catalysis, and specifically relates to a platinum-nickel nanocrystal-modified carbon-based catalyst and a gram-level low-pressure preparation method and application thereof.
背景技术Background Art
质子交换膜燃料电池(PEMFC)是具有较大潜力的清洁能源,但其性能受到氧还原反应(ORR)的较大限制。燃料电池一直被认为是最高效、最清洁的能源转换装置,燃料与氧通过温和的电化学过程发生反应而不燃烧,可以在接近室温的条件下将氢或烃类中蕴含的巨大化学能通过电化学途径直接转化为清洁、稳定、可持续的电能,因而被视为极有前景的、能够满足日益增长的世界能源需求的解决方案之一。然而,在实际应用中,低温燃料电池并没有表现出这样的效率,主要是由于阴极的氧还原反应缓慢。在一个典型的氢燃料电池中,氢在正极氧化而氧在负极还原,从动力学角度说,氧还原反应比氢氧化反应进行的慢,因此氧还原反应成为了制约燃料电池发展的一个重要因素。在众多催化剂中,贵金属铂基催化剂在ORR反应中具有极高的活性,应用前景广泛。但铂基催化剂在燃料电池中的广泛应用存在一些缺陷。主要原因是铂的供应非常有限,价格高昂,并且批量制备较为困难,不适用于大规模的工业应用;因此,合理设计低铂载量、稳定性高的铂基催化剂,以及可大规模合成产物的制备方法在实际应用中具有重要意义。Proton exchange membrane fuel cells (PEMFCs) are clean energy with great potential, but their performance is greatly limited by the oxygen reduction reaction (ORR). Fuel cells have always been considered the most efficient and cleanest energy conversion devices. Fuel and oxygen react through a mild electrochemical process without combustion. The huge chemical energy contained in hydrogen or hydrocarbons can be directly converted into clean, stable and sustainable electricity through electrochemical pathways at near room temperature. Therefore, they are regarded as one of the most promising solutions to meet the growing world energy needs. However, in practical applications, low-temperature fuel cells do not show such efficiency, mainly due to the slow oxygen reduction reaction at the cathode. In a typical hydrogen fuel cell, hydrogen is oxidized at the positive electrode and oxygen is reduced at the negative electrode. From a kinetic point of view, the oxygen reduction reaction is slower than the hydrogen oxidation reaction, so the oxygen reduction reaction has become an important factor restricting the development of fuel cells. Among many catalysts, precious metal platinum-based catalysts have extremely high activity in the ORR reaction and have broad application prospects. However, there are some defects in the widespread use of platinum-based catalysts in fuel cells. The main reason is that the supply of platinum is very limited, the price is high, and batch preparation is difficult, making it unsuitable for large-scale industrial applications. Therefore, the rational design of platinum-based catalysts with low platinum loading and high stability, as well as preparation methods that can synthesize products on a large scale are of great significance in practical applications.
通过不同金属的掺杂,不仅会改变贵金属铂的电子结构,使得其具有更佳的氧还原反应性能。并且将铂镍纳米晶颗粒负载在高活性碳载体上可在降低贵金属铂含量的同时,提高反应过程中的电子传输速率。该合成方法简单便捷,在稳定剂的作用下,可在常压下将催化剂的产量提高到克级,并且在低铂含量下,提高了氧还原反应性能。该技术能够将催化剂的产量从毫克级别提高到克级,并且低铂含量大大降低铂基催化剂的生产成本,为燃料电池的大规模商业化应用提供了一定基础。By doping with different metals, not only will the electronic structure of the precious metal platinum be changed, making it have better oxygen reduction reaction performance. And loading platinum-nickel nanocrystalline particles on a highly active carbon carrier can reduce the content of precious metal platinum while increasing the electron transfer rate during the reaction. This synthesis method is simple and convenient. Under the action of a stabilizer, the output of the catalyst can be increased to the gram level at normal pressure, and the oxygen reduction reaction performance is improved at a low platinum content. This technology can increase the output of the catalyst from the milligram level to the gram level, and the low platinum content greatly reduces the production cost of platinum-based catalysts, providing a certain basis for the large-scale commercial application of fuel cells.
发明内容Summary of the invention
本发明的主要目的在于提供一种铂镍纳米晶修饰碳基催化剂及其克级低压制备方法与应用,以克服现有技术的不足。The main purpose of the present invention is to provide a platinum-nickel nanocrystal modified carbon-based catalyst and a gram-level low-pressure preparation method and application thereof, so as to overcome the shortcomings of the prior art.
为实现前述发明目的,本发明采用的技术方案包括:In order to achieve the above-mentioned invention object, the technical solution adopted by the present invention includes:
本发明实施例提供了一种铂镍纳米晶修饰碳基催化剂的克级低压制备方法,其包括:使包含铂前驱体、镍前驱体、炭黑、稳定剂、结构导向剂和溶剂的混合反应体系于130~210℃常压反应12h,制得铂镍纳米晶修饰碳基催化剂。An embodiment of the present invention provides a gram-level low-pressure preparation method for a platinum-nickel nanocrystal modified carbon-based catalyst, which comprises: reacting a mixed reaction system comprising a platinum precursor, a nickel precursor, carbon black, a stabilizer, a structure directing agent and a solvent at 130-210° C. and normal pressure for 12 hours to obtain a platinum-nickel nanocrystal modified carbon-based catalyst.
本发明实施例还提供了前述的克级低压制备方法制得的铂镍纳米晶修饰碳基催化剂,所述铂镍纳米晶修饰碳基催化剂中PtNi颗粒的粒径为3~4nm;所述铂镍纳米晶修饰碳基催化剂中的Pt的含量为3.00~3.36wt%。The embodiment of the present invention also provides a platinum-nickel nanocrystal modified carbon-based catalyst prepared by the aforementioned gram-level low-pressure preparation method, wherein the particle size of the PtNi particles in the platinum-nickel nanocrystal modified carbon-based catalyst is 3 to 4 nm; the Pt content in the platinum-nickel nanocrystal modified carbon-based catalyst is 3.00 to 3.36 wt%.
本发明实施例还提供了前述的铂镍纳米晶修饰碳基催化剂于制备燃料电池中的应用。The embodiment of the present invention also provides the use of the aforementioned platinum-nickel nanocrystal modified carbon-based catalyst in the preparation of a fuel cell.
与现有技术相比,本发明的有益效果在于:Compared with the prior art, the present invention has the following beneficial effects:
(1)本发明在结构导向剂及稳定剂的作用下,将铂镍前驱体负载在碳基载体上,所合成的铂镍纳米晶修饰碳基催化剂中的PtNi颗粒粒径在3-4nm,铂含量仅为3.00~3.36wt%,且铂镍纳米晶修饰碳基催化剂的氧还原反应中比活性分别为商用Pt/C-5%(Pt含量为5%)、Pt/C-20%(Pt含量为20%)催化剂的9.28、6.47倍;(1) In the present invention, under the action of a structure directing agent and a stabilizer, a platinum-nickel precursor is loaded on a carbon-based carrier, and the PtNi particle size of the synthesized platinum-nickel nanocrystal modified carbon-based catalyst is 3-4 nm, and the platinum content is only 3.00-3.36 wt %. In addition, the specific activity of the platinum-nickel nanocrystal modified carbon-based catalyst in the oxygen reduction reaction is 9.28 and 6.47 times that of the commercial Pt/C-5% (Pt content is 5%) and Pt/C-20% (Pt content is 20%) catalysts, respectively;
(2)本发明中的铂镍纳米晶修饰碳基催化剂可在常压下进行,具有铂含量低、氧还原性能优异、稳定性高、且可克级生产制备等优点,可大幅度降低生产成本,具有十分广泛的工业化应用前景。(2) The platinum-nickel nanocrystal-modified carbon-based catalyst in the present invention can be produced under normal pressure, has the advantages of low platinum content, excellent oxygen reduction performance, high stability, and can be produced and prepared at the gram level, which can greatly reduce the production cost and has a very broad prospect for industrial application.
附图说明BRIEF DESCRIPTION OF THE DRAWINGS
为了更清楚地说明本发明实施例或现有技术中的技术方案,下面将对实施例或现有技术描述中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图仅仅是本发明中记载的一些实施例,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据这些附图获得其他的附图。In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings required for use in the embodiments or the description of the prior art will be briefly introduced below. Obviously, the drawings described below are only some embodiments recorded in the present invention. For ordinary technicians in this field, other drawings can be obtained based on these drawings without paying creative work.
图1是本实施例1中铂镍纳米晶修饰碳基催化剂PtNi/C的扫描电子显微图;FIG1 is a scanning electron micrograph of a platinum-nickel nanocrystal-modified carbon-based catalyst PtNi/C in Example 1;
图2是本实施例1中铂镍纳米晶修饰碳基催化剂PtNi/C的透射电子显微图;FIG2 is a transmission electron micrograph of the carbon-based catalyst PtNi/C modified with platinum-nickel nanocrystals in Example 1;
图3是本实施例1中铂镍纳米晶修饰碳基催化剂PtNi/C的XRD谱图;FIG3 is an XRD spectrum of the carbon-based catalyst PtNi/C modified with platinum-nickel nanocrystals in Example 1;
图4是本实施例1中克级合成制备装置的示意图;FIG4 is a schematic diagram of a gram-scale synthesis preparation device in Example 1;
图5是本发明实施例1-6中不同温度下所合成PtNi/C催化剂在碱性溶液(0.1M氢氧化钾)中氧还原反应性能测试的结果图;5 is a graph showing the results of oxygen reduction reaction performance tests of the PtNi/C catalysts synthesized at different temperatures in alkaline solutions (0.1 M potassium hydroxide) in Examples 1-6 of the present invention;
图6是本发明实施例7-11中不同铂镍比例所合成PtNi/C催化剂在碱性溶液(0.1M氢氧化钾)中氧还原反应性能测试的结果图;6 is a graph showing the results of oxygen reduction reaction performance tests of PtNi/C catalysts synthesized with different platinum-nickel ratios in Examples 7-11 of the present invention in an alkaline solution (0.1 M potassium hydroxide);
图7是本发明实施例10中的PtNi/C-200℃-Pt∶Ni=1∶2、及对比例1中商业Pt/C-5%、商业Pt/C-20%的氧还原反应性能测试图;7 is a graph showing the oxygen reduction reaction performance of PtNi/C-200°C-Pt:Ni=1:2 in Example 10 of the present invention and commercial Pt/C-5% and commercial Pt/C-20% in Comparative Example 1;
图8是本发明对比例2制备的催化剂的透射电子显微图;FIG8 is a transmission electron micrograph of the catalyst prepared in Comparative Example 2 of the present invention;
图9是本发明对比例3制备的催化剂的透射电子显微图;FIG9 is a transmission electron micrograph of the catalyst prepared in Comparative Example 3 of the present invention;
图10是本发明对比例4制备的催化剂的透射电子显微图;FIG10 is a transmission electron micrograph of the catalyst prepared in Comparative Example 4 of the present invention;
图11本发明对比例2-4制备的催化剂的氧还原反应性能测试图。FIG. 11 is a graph showing the oxygen reduction reaction performance test of the catalysts prepared in Comparative Examples 2-4 of the present invention.
具体实施方式DETAILED DESCRIPTION
鉴于现有技术的缺陷,本案发明人经长期研究和大量实践,得以提出本发明的技术方案,本发明为解决现有商业铂基催化剂制备成本较高的问题,公开了一种铂镍纳米晶修饰碳基催化剂的克级低压制备方法。所述合成方法在常温下可实现催化剂的克级制备,并且通过低铂载量的铂镍纳米晶对碳基进行修饰,达到了优异的催化性能。该制备方法简单易行,所合成纳米晶尺寸为3-4nm,在碳基载体上分散均匀,具有极高的稳定性。In view of the defects of the prior art, the inventors of this case have proposed the technical solution of the present invention after long-term research and extensive practice. In order to solve the problem of high preparation cost of existing commercial platinum-based catalysts, the present invention discloses a gram-level low-pressure preparation method of a carbon-based catalyst modified with platinum-nickel nanocrystals. The synthesis method can achieve gram-level preparation of catalysts at room temperature, and the carbon base is modified by platinum-nickel nanocrystals with low platinum loading, thereby achieving excellent catalytic performance. The preparation method is simple and easy, and the synthesized nanocrystals have a size of 3-4nm, are evenly dispersed on the carbon-based carrier, and have extremely high stability.
利用副族元素镍与贵金属铂形成合金,改变贵金属铂的电子结构,提高了贵金属铂在氧还原反应过程中的催化性能;镍与铂形成合金并负载在碳载体上,使得所形成的合金分布更加均匀,提高了铂原子的利用率,有效的降低了氧还原催化剂中贵金属铂的含量,从而降低了工业化应用的成本。在苯甲酸和十六烷基三甲基溴化铵的作用下,可在常压下形成稳定的铂镍纳米晶,尺寸小且不易聚集。通过该种合成方法,将催化剂的产量从毫克级提高到了克级,对燃料电池进一步商业化应用具有重要意义。By using the subgroup element nickel and the precious metal platinum to form an alloy, the electronic structure of the precious metal platinum is changed, and the catalytic performance of the precious metal platinum in the oxygen reduction reaction process is improved; nickel and platinum form an alloy and are loaded on a carbon carrier, so that the distribution of the formed alloy is more uniform, the utilization rate of platinum atoms is improved, and the content of precious metal platinum in the oxygen reduction catalyst is effectively reduced, thereby reducing the cost of industrial application. Under the action of benzoic acid and hexadecyltrimethylammonium bromide, stable platinum-nickel nanocrystals with small size and not easy to aggregate can be formed under normal pressure. Through this synthesis method, the output of the catalyst is increased from milligrams to grams, which is of great significance for the further commercial application of fuel cells.
下面将对本发明的技术方案进行清楚、完整地描述,显然,所描述的实施例是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。The technical solution of the present invention will be described clearly and completely below. Obviously, the described embodiments are only part of the embodiments of the present invention, not all of them. Based on the embodiments of the present invention, all other embodiments obtained by ordinary technicians in this field without creative work are within the scope of protection of the present invention.
具体的,作为本发明技术方案的一个方面,其所涉及的一种铂镍纳米晶修饰碳基催化剂的克级低压制备方法包括:使包含铂前驱体、镍前驱体、炭黑、稳定剂、结构导向剂和溶剂的混合反应体系于130~210℃常压反应12h,制得铂镍纳米晶修饰碳基催化剂。Specifically, as one aspect of the technical solution of the present invention, a gram-level low-pressure preparation method of a platinum-nickel nanocrystal modified carbon-based catalyst involves: reacting a mixed reaction system comprising a platinum precursor, a nickel precursor, carbon black, a stabilizer, a structure directing agent and a solvent at 130-210°C under normal pressure for 12 hours to obtain a platinum-nickel nanocrystal modified carbon-based catalyst.
在一些优选实施方案中,所述克级低压制备方法包括:将铂前驱体、镍前驱体、炭黑、稳定剂、结构导向剂分散于溶剂中形成所述混合反应体系。In some preferred embodiments, the gram-scale low-pressure preparation method comprises: dispersing a platinum precursor, a nickel precursor, carbon black, a stabilizer, and a structure directing agent in a solvent to form the mixed reaction system.
在一些优选实施方案中,所述铂前驱体包括乙酰丙酮铂和/或四氯合铂酸钾,且不限于此。In some preferred embodiments, the platinum precursor includes platinum acetylacetonate and/or potassium tetrachloroplatinate, but is not limited thereto.
在一些优选实施方案中,所述镍前驱体包括乙酰丙酮镍和/或氯化镍,且不限于此。In some preferred embodiments, the nickel precursor includes nickel acetylacetonate and/or nickel chloride, but is not limited thereto.
在一些优选实施方案中,所述稳定剂包括苯甲酸,且不限于此。In some preferred embodiments, the stabilizer includes benzoic acid, but is not limited thereto.
在一些优选实施方案中,所述结构导向剂包括十六烷基三甲基溴化铵,其中所述十六烷基三甲基溴化铵作用在于稳定PtNi纳米晶,并控制其颗粒粒径,形成较小尺寸的PtNi纳米颗粒。In some preferred embodiments, the structure directing agent includes hexadecyltrimethylammonium bromide, wherein the hexadecyltrimethylammonium bromide functions to stabilize PtNi nanocrystals and control their particle size to form PtNi nanoparticles of smaller size.
在一些优选实施方案中,所述炭黑包括Vulcan XC-72、科琴黑、乙炔黑中的任意一种或两种以上的组合,且不限于此。In some preferred embodiments, the carbon black includes any one of Vulcan XC-72, Ketjen black, and acetylene black, or a combination of two or more thereof, but is not limited thereto.
在一些优选实施方案中,所述溶剂包括苯甲醇,且不限于此。In some preferred embodiments, the solvent includes benzyl alcohol, but is not limited thereto.
在一些优选实施方案中,所述铂前驱体与镍前驱体的质量比为3∶1~1∶3。In some preferred embodiments, the mass ratio of the platinum precursor to the nickel precursor is 3:1 to 1:3.
在一些优选实施方案中,所述炭黑与铂前驱体的质量比为11.25∶1。In some preferred embodiments, the mass ratio of the carbon black to the platinum precursor is 11.25:1.
在一些优选实施方案中,所述稳定剂与铂前驱体的质量比为6.25∶1。In some preferred embodiments, the mass ratio of the stabilizer to the platinum precursor is 6.25:1.
在一些优选实施方案中,所述结构导向剂与铂前驱体的质量比为10.00∶1。In some preferred embodiments, the mass ratio of the structure directing agent to the platinum precursor is 10.00:1.
在一些优选实施方案中,所述克级低压制备方法还包括:在所述反应完成后,对所获产物进行洗涤、离心、干燥处理。In some preferred embodiments, the gram-scale low-pressure preparation method further comprises: after the reaction is completed, washing, centrifuging and drying the obtained product.
进一步地,采用乙醇与丙酮对所获产物进行洗涤、离心处理。Furthermore, the obtained product is washed with ethanol and acetone and centrifuged.
在一些更为具体的实施方案中,所述铂镍纳米晶修饰碳基催化剂的克级低压制备方法包括:In some more specific embodiments, the gram-scale low-pressure preparation method of the platinum-nickel nanocrystal modified carbon-based catalyst comprises:
(1)称量不同比例铂前驱体、镍前驱体,在稳定剂、结构导向剂的作用下,于室温下搅拌为均一溶液;(1) weighing different proportions of platinum precursor and nickel precursor, stirring at room temperature to form a uniform solution under the action of a stabilizer and a structure directing agent;
(2)将步骤(1)所述溶液置于油浴装置内,设置反应温度,在常压下制备样品;(2) placing the solution of step (1) in an oil bath, setting the reaction temperature, and preparing a sample under normal pressure;
(3)在步骤(2)中所合成的样品中,加入乙醇与丙酮对样品进行清洗离心;(3) adding ethanol and acetone to the sample synthesized in step (2) to wash and centrifuge the sample;
(4)将步骤(3)中离心所得样品置于真空干燥箱中进行干燥处理,制得铂镍纳米晶修饰碳基催化剂。(4) The sample obtained by centrifugation in step (3) is placed in a vacuum drying oven for drying to obtain a platinum-nickel nanocrystal-modified carbon-based catalyst.
进一步地,在步骤(2)中,反应温度为:130℃或150℃或170℃或190℃或200℃或210℃中的任一者。Furthermore, in step (2), the reaction temperature is any one of 130°C, 150°C, 170°C, 190°C, 200°C or 210°C.
本发明实施例的另一个方面还提供了前述的克级低压制备方法制得的铂镍纳米晶修饰碳基催化剂,所述铂镍纳米晶修饰碳基催化剂中PtNi颗粒的粒径为3~4nm;所述铂镍纳米晶修饰碳基催化剂中的Pt的含量为3.00~3.36wt%,优选为3.04%。Another aspect of an embodiment of the present invention further provides a platinum-nickel nanocrystal-modified carbon-based catalyst prepared by the aforementioned gram-level low-pressure preparation method, wherein the particle size of the PtNi particles in the platinum-nickel nanocrystal-modified carbon-based catalyst is 3 to 4 nm; the Pt content in the platinum-nickel nanocrystal-modified carbon-based catalyst is 3.00 to 3.36 wt%, preferably 3.04%.
本发明实施例的另一个方面还提供了前述的铂镍纳米晶修饰碳基催化剂于制备燃料电池中的应用。Another aspect of the embodiments of the present invention further provides the use of the aforementioned platinum-nickel nanocrystal modified carbon-based catalyst in the preparation of a fuel cell.
下面结合若干优选实施例及附图对本发明的技术方案做进一步详细说明,本实施例在以发明技术方案为前提下进行实施,给出了详细的实施方式和具体的操作过程,但本发明的保护范围不限于下述的实施例。The technical solution of the present invention is further described in detail below in conjunction with several preferred embodiments and drawings. This embodiment is implemented on the premise of the technical solution of the invention, and a detailed implementation method and specific operation process are given, but the protection scope of the present invention is not limited to the following embodiments.
下面所用的实施例中所采用的实验材料,如无特殊说明,均可由常规的生化试剂公司购买得到。Unless otherwise specified, the experimental materials used in the following examples can be purchased from conventional biochemical reagent companies.
实施例1Example 1
(1)将90mg炭黑(Vulcan XC-72)、10.28mg乙酰丙酮镍、80mg十六烷基三甲基溴化铵、50mg苯甲酸、8mg乙酰丙酮铂溶于5mL溶剂中,搅拌至溶液均一。后将溶液转移至油浴装置中,在130℃下反应12h;(1) Dissolve 90 mg of carbon black (Vulcan XC-72), 10.28 mg of nickel acetylacetonate, 80 mg of hexadecyltrimethylammonium bromide, 50 mg of benzoic acid, and 8 mg of platinum acetylacetonate in 5 mL of solvent and stir until the solution is uniform. Then transfer the solution to an oil bath and react at 130°C for 12 h.
(2)将步骤(1)所合成产物用乙醇与丙酮洗涤,随后离心分离出固态产物;(2) washing the product synthesized in step (1) with ethanol and acetone, and then centrifuging to separate the solid product;
(3)将步骤(2)所合成样品在干燥箱中干燥12h,得到铂镍纳米晶修饰碳基催化剂PtNi/C(记为:合成PtNi/C-130℃)。该温度下所合成PtNi/C催化剂对氧还原反应催化性能较优。本实施例中PtNi/C催化剂的产量为1.15g。(3) The sample synthesized in step (2) was dried in a drying oven for 12 hours to obtain a platinum-nickel nanocrystal modified carbon-based catalyst PtNi/C (recorded as: synthesized PtNi/C-130°C). The synthesized PtNi/C catalyst at this temperature has a better catalytic performance for oxygen reduction reaction. The yield of the PtNi/C catalyst in this example is 1.15 g.
图1是本实施例中铂镍纳米晶修饰碳基催化剂PtNi/C的扫描电子显微图;图2是本实施例中铂镍纳米晶修饰碳基催化剂PtNi/C的透射电子显微图;图3是本实施例中铂镍纳米晶修饰碳基催化剂PtNi/C的XRD谱图;图4是本实施例克级合成制备装置示意图。Figure 1 is a scanning electron micrograph of the platinum-nickel nanocrystal-modified carbon-based catalyst PtNi/C in this embodiment; Figure 2 is a transmission electron micrograph of the platinum-nickel nanocrystal-modified carbon-based catalyst PtNi/C in this embodiment; Figure 3 is an XRD spectrum of the platinum-nickel nanocrystal-modified carbon-based catalyst PtNi/C in this embodiment; Figure 4 is a schematic diagram of the gram-level synthesis preparation device in this embodiment.
实施例2Example 2
(1)将90mg炭黑(Vulcan XC-72)、10.28mg乙酰丙酮镍、80mg十六烷基三甲基溴化铵、50mg苯甲酸、8mg乙酰丙酮铂溶于5mL溶剂中,搅拌至溶液均一。后将溶液转移至油浴装置中,在150℃下反应12h;(1) Dissolve 90 mg of carbon black (Vulcan XC-72), 10.28 mg of nickel acetylacetonate, 80 mg of hexadecyltrimethylammonium bromide, 50 mg of benzoic acid, and 8 mg of platinum acetylacetonate in 5 mL of solvent and stir until the solution is uniform. Then transfer the solution to an oil bath and react at 150°C for 12 h.
(2)将步骤(1)所合成产物用乙醇与丙酮洗涤,随后离心分离出固态产物;(2) washing the product synthesized in step (1) with ethanol and acetone, and then centrifuging to separate the solid product;
(3)将步骤(2)所合成样品在干燥箱中干燥12h,得到铂镍纳米晶修饰碳基催化剂PtNi/C(记为:合成PtNi/C-150℃)。该温度下所合成PtNi/C催化剂对氧还原反应催化性能较优。(3) The sample synthesized in step (2) was dried in a drying oven for 12 hours to obtain a platinum-nickel nanocrystal-modified carbon-based catalyst PtNi/C (recorded as: synthesized PtNi/C-150°C). The PtNi/C catalyst synthesized at this temperature has a better catalytic performance for oxygen reduction reaction.
实施例3Example 3
(1)将90mg炭黑(Vulcan XC-72)、10.28mg乙酰丙酮镍、80mg十六烷基三甲基溴化铵、50mg苯甲酸、8mg乙酰丙酮铂溶于5mL溶剂中,搅拌至溶液均一。后将溶液转移至油浴装置中,在170℃下反应12h;(1) Dissolve 90 mg of carbon black (Vulcan XC-72), 10.28 mg of nickel acetylacetonate, 80 mg of hexadecyltrimethylammonium bromide, 50 mg of benzoic acid, and 8 mg of platinum acetylacetonate in 5 mL of solvent and stir until the solution is uniform. Then transfer the solution to an oil bath and react at 170°C for 12 h.
(2)将步骤(1)所合成产物用乙醇与丙酮洗涤,随后离心分离出固态产物;(2) washing the product synthesized in step (1) with ethanol and acetone, and then centrifuging to separate the solid product;
(3)将步骤(2)所合成样品在干燥箱中干燥12h,得到铂镍纳米晶修饰碳基催化剂PtNi/C(记为:合成PtNi/C-170℃)。该温度下所合成PtNi/C催化剂对氧还原反应催化性能较优。(3) The sample synthesized in step (2) was dried in a drying oven for 12 hours to obtain a platinum-nickel nanocrystal-modified carbon-based catalyst PtNi/C (recorded as: synthesized PtNi/C-170°C). The PtNi/C catalyst synthesized at this temperature has a better catalytic performance for oxygen reduction reaction.
实施例4Example 4
(1)将90mg炭黑(Vulcan XC-72)、10.28mg乙酰丙酮镍、80mg十六烷基三甲基溴化铵、50mg苯甲酸、8mg乙酰丙酮铂溶于5mL溶剂中,搅拌至溶液均一。后将溶液转移至油浴装置中,在190℃下反应12h;(1) Dissolve 90 mg of carbon black (Vulcan XC-72), 10.28 mg of nickel acetylacetonate, 80 mg of hexadecyltrimethylammonium bromide, 50 mg of benzoic acid, and 8 mg of platinum acetylacetonate in 5 mL of solvent and stir until the solution is uniform. Then transfer the solution to an oil bath and react at 190°C for 12 h.
(2)将步骤(1)所合成产物用乙醇与丙酮洗涤,随后离心分离出固态产物;(2) washing the product synthesized in step (1) with ethanol and acetone, and then centrifuging to separate the solid product;
(3)将步骤(2)所合成样品在干燥箱中干燥12h,得到铂镍纳米晶修饰碳基催化剂PtNi/C(记为:合成PtNi/C-190℃)。该温度下所合成PtNi/C催化剂对氧还原反应催化性能较优。(3) The sample synthesized in step (2) was dried in a drying oven for 12 hours to obtain a platinum-nickel nanocrystal-modified carbon-based catalyst PtNi/C (recorded as: synthesized PtNi/C-190°C). The PtNi/C catalyst synthesized at this temperature has a better catalytic performance for oxygen reduction reaction.
实施例5Example 5
(1)将90mg炭黑(Vulcan XC-72)、10.28mg乙酰丙酮镍、80mg十六烷基三甲基溴化铵、50mg苯甲酸、8mg乙酰丙酮铂溶于5mL溶剂中,搅拌至溶液均一。后将溶液转移至油浴装置中,在200℃下反应12h;(1) Dissolve 90 mg of carbon black (Vulcan XC-72), 10.28 mg of nickel acetylacetonate, 80 mg of hexadecyltrimethylammonium bromide, 50 mg of benzoic acid, and 8 mg of platinum acetylacetonate in 5 mL of solvent and stir until the solution is uniform. Then transfer the solution to an oil bath and react at 200°C for 12 h.
(2)将步骤(1)所合成产物用乙醇与丙酮洗涤,随后离心分离出固态产物;(2) washing the product synthesized in step (1) with ethanol and acetone, and then centrifuging to separate the solid product;
(3)将步骤(2)所合成样品在干燥箱中干燥12h,得到铂镍纳米晶修饰碳基催化剂PtNi/C(记为:合成PtNi/C-200℃)该温度下所合成PtNi/C催化剂对氧还原反应催化性能较优。(3) Dry the sample synthesized in step (2) in a drying oven for 12 hours to obtain a platinum-nickel nanocrystal-modified carbon-based catalyst PtNi/C (denoted as: synthesized PtNi/C-200°C). The PtNi/C catalyst synthesized at this temperature has better catalytic performance for oxygen reduction reaction.
实施例6Example 6
(1)将90mg炭黑(Vulcan XC-72)、10.28mg乙酰丙酮镍、80mg十六烷基三甲基溴化铵、50mg苯甲酸、8mg乙酰丙酮铂溶于5mL溶剂中,搅拌至溶液均一。后将溶液转移至油浴装置中,在210℃下反应12h;(1) Dissolve 90 mg of carbon black (Vulcan XC-72), 10.28 mg of nickel acetylacetonate, 80 mg of hexadecyltrimethylammonium bromide, 50 mg of benzoic acid, and 8 mg of platinum acetylacetonate in 5 mL of solvent and stir until the solution is uniform. Then transfer the solution to an oil bath and react at 210°C for 12 h.
(2)将步骤(1)所合成产物用乙醇与丙酮洗涤,随后离心分离出固态产物;(2) washing the product synthesized in step (1) with ethanol and acetone, and then centrifuging to separate the solid product;
(3)将步骤(2)所合成样品在干燥箱中干燥12h,得到铂镍纳米晶修饰碳基催化剂PtNi/C(记为:合成PtNi/C-210℃)该温度下所合成PtNi/C催化剂对氧还原反应催化性能较优。(3) Dry the sample synthesized in step (2) in a drying oven for 12 hours to obtain a platinum-nickel nanocrystal-modified carbon-based catalyst PtNi/C (denoted as: synthesized PtNi/C-210°C). The PtNi/C catalyst synthesized at this temperature has better catalytic performance for oxygen reduction reaction.
图5是本发明实施例1-6中不同温度下所合成PtNi/C催化剂在碱性溶液(0.1M氢氧化钾)中氧还原反应性能测试的结果。通过对比发现,在温度从130℃增加到200℃时,随着合成样品时温度的增加,催化氧还原反应性能测试的结果越好,在温度升高到210℃时,合成样品时温度对氧还原反应性能相对于200℃时所合成PtNi/C催化剂略差,但依旧对氧还原反应具有优异的催化剂活性。因此,200℃时所合成的PtNi/C催化剂为合成样品的最优温度。Figure 5 is the results of the oxygen reduction reaction performance test of the PtNi/C catalyst synthesized at different temperatures in Examples 1-6 of the present invention in an alkaline solution (0.1M potassium hydroxide). By comparison, it was found that when the temperature increased from 130°C to 200°C, as the temperature increased during the synthesis of the sample, the results of the catalytic oxygen reduction reaction performance test became better. When the temperature was raised to 210°C, the temperature during the synthesis of the sample had a slightly worse oxygen reduction reaction performance than the PtNi/C catalyst synthesized at 200°C, but it still had excellent catalytic activity for the oxygen reduction reaction. Therefore, the PtNi/C catalyst synthesized at 200°C is the optimal temperature for the synthesis of the sample.
本发明中不同温度所合成PtNi/C催化剂在酸性溶液(0.1M高氯酸)中显示出优异的氧还原反应催化性能。并在所探究的不同温度(130℃或150℃或170℃或190℃或200℃或210℃)条件下,所合成的催化剂都显示出对氧还原反应优异的催化活性。The PtNi/C catalysts synthesized at different temperatures in the present invention show excellent catalytic performance for oxygen reduction reaction in an acidic solution (0.1M perchloric acid). And under the different temperatures investigated (130°C, 150°C, 170°C, 190°C, 200°C, or 210°C), the synthesized catalysts all show excellent catalytic activity for oxygen reduction reaction.
实施例7Example 7
(1)将90mg炭黑(Vulcan XC-72)、1.742mg乙酰丙酮镍、80mg十六烷基三甲基溴化铵、50mg苯甲酸、8mg乙酰丙酮铂溶于5mL苯甲醇中,搅拌至溶液均一。后将溶液转移至油浴装置中,在200℃下反应12h;(1) Dissolve 90 mg of carbon black (Vulcan XC-72), 1.742 mg of nickel acetylacetonate, 80 mg of hexadecyltrimethylammonium bromide, 50 mg of benzoic acid, and 8 mg of platinum acetylacetonate in 5 mL of benzyl alcohol and stir until the solution is uniform. Then transfer the solution to an oil bath and react at 200°C for 12 h.
(2)将步骤(1)所合成产物用乙醇与丙酮洗涤,随后离心分离出固态产物;(2) washing the product synthesized in step (1) with ethanol and acetone, and then centrifuging to separate the solid product;
(3)将步骤(2)所合成样品在干燥箱中干燥12h,得到铂镍纳米晶修饰碳基催化剂PtNi/C(记为:合成PtNi/C-200℃-Pt∶Ni=3∶1)。铂镍纳米晶修饰碳基催化剂PtNi/C的组成如表1所示。(3) The sample synthesized in step (2) was dried in a drying oven for 12 hours to obtain a platinum-nickel nanocrystal modified carbon-based catalyst PtNi/C (recorded as: synthesized PtNi/C-200°C-Pt:Ni=3:1). The composition of the platinum-nickel nanocrystal modified carbon-based catalyst PtNi/C is shown in Table 1.
实施例8Example 8
(1)将90mg炭黑(Vulcan XC-72)、2.613mg乙酰丙酮镍、80mg十六烷基三甲基溴化铵、50mg苯甲酸、8mg乙酰丙酮铂溶于5mL苯甲醇中,搅拌至溶液均一。后将溶液转移至油浴装置中,在200℃下反应12h;(1) Dissolve 90 mg of carbon black (Vulcan XC-72), 2.613 mg of nickel acetylacetonate, 80 mg of hexadecyltrimethylammonium bromide, 50 mg of benzoic acid, and 8 mg of platinum acetylacetonate in 5 mL of benzyl alcohol and stir until the solution is uniform. Then transfer the solution to an oil bath and react at 200°C for 12 h.
(2)将步骤(1)所合成产物用乙醇与丙酮洗涤,随后离心分离出固态产物;(2) washing the product synthesized in step (1) with ethanol and acetone, and then centrifuging to separate the solid product;
(3)将步骤(2)所合成样品在干燥箱中干燥12h,得到铂镍纳米晶修饰碳基催化剂PtNi/C(记为:合成PtNi/C-200℃-Pt∶Ni=2∶1)。铂镍纳米晶修饰碳基催化剂PtNi/C的组成如表1所示。(3) The sample synthesized in step (2) was dried in a drying oven for 12 hours to obtain a platinum-nickel nanocrystal modified carbon-based catalyst PtNi/C (recorded as: synthesized PtNi/C-200°C-Pt:Ni=2:1). The composition of the platinum-nickel nanocrystal modified carbon-based catalyst PtNi/C is shown in Table 1.
实施例9Example 9
(1)将90mg炭黑(Vulcan XC-72)、5.203mg乙酰丙酮镍、80mg十六烷基三甲基溴化铵、50mg苯甲酸、8mg乙酰丙酮铂溶于5mL苯甲醇中,搅拌至溶液均一。后将溶液转移至油浴装置中,在200℃下反应12h;(1) Dissolve 90 mg of carbon black (Vulcan XC-72), 5.203 mg of nickel acetylacetonate, 80 mg of hexadecyltrimethylammonium bromide, 50 mg of benzoic acid, and 8 mg of platinum acetylacetonate in 5 mL of benzyl alcohol and stir until the solution is uniform. Then transfer the solution to an oil bath and react at 200°C for 12 h.
(2)将步骤(1)所合成产物用乙醇与丙酮洗涤,随后离心分离出固态产物;(2) washing the product synthesized in step (1) with ethanol and acetone, and then centrifuging to separate the solid product;
(3)将步骤(2)所合成样品在干燥箱中干燥12h,得到铂镍纳米晶修饰碳基催化剂PtNi/C(记为:合成PtNi/C-200℃-Pt∶Ni=1∶1)。铂镍纳米晶修饰碳基催化剂PtNi/C的组成如表1所示。(3) The sample synthesized in step (2) was dried in a drying oven for 12 hours to obtain a platinum-nickel nanocrystal modified carbon-based catalyst PtNi/C (recorded as: synthesized PtNi/C-200°C-Pt:Ni=1:1). The composition of the platinum-nickel nanocrystal modified carbon-based catalyst PtNi/C is shown in Table 1.
实施例10Example 10
(1)将90mg炭黑(Vulcan XC-72)、10.451mg乙酰丙酮镍、80mg十六烷基三甲基溴化铵、50mg苯甲酸、8mg乙酰丙酮铂溶于5mL苯甲醇中,搅拌至溶液均一。后将溶液转移至油浴装置中,在200℃下反应12h;(1) Dissolve 90 mg of carbon black (Vulcan XC-72), 10.451 mg of nickel acetylacetonate, 80 mg of hexadecyltrimethylammonium bromide, 50 mg of benzoic acid, and 8 mg of platinum acetylacetonate in 5 mL of benzyl alcohol and stir until the solution is uniform. Then transfer the solution to an oil bath and react at 200°C for 12 h.
(2)将步骤(1)所合成产物用乙醇与丙酮洗涤,随后离心分离出固态产物;(2) washing the product synthesized in step (1) with ethanol and acetone, and then centrifuging to separate the solid product;
(3)将步骤(2)所合成样品在干燥箱中干燥12h,得到铂镍纳米晶修饰碳基催化剂PtNi/C(记为:合成PtNi/C-200℃-Pt∶Ni=1∶2)。铂镍纳米晶修饰碳基催化剂PtNi/C的组成如表1所示。(3) The sample synthesized in step (2) was dried in a drying oven for 12 hours to obtain a platinum-nickel nanocrystal modified carbon-based catalyst PtNi/C (recorded as: synthesized PtNi/C-200°C-Pt:Ni=1:2). The composition of the platinum-nickel nanocrystal modified carbon-based catalyst PtNi/C is shown in Table 1.
实施例11Embodiment 11
(1)将90mg炭黑(Vulcan XC-72)、15.677mg乙酰丙酮镍、80mg十六烷基三甲基溴化铵、50mg苯甲酸、8mg乙酰丙酮铂溶于5mL苯甲醇中,搅拌至溶液均一。后将溶液转移至油浴装置中,在200℃下反应12h;(1) Dissolve 90 mg of carbon black (Vulcan XC-72), 15.677 mg of nickel acetylacetonate, 80 mg of hexadecyltrimethylammonium bromide, 50 mg of benzoic acid, and 8 mg of platinum acetylacetonate in 5 mL of benzyl alcohol and stir until the solution is uniform. Then transfer the solution to an oil bath and react at 200°C for 12 h.
(2)将步骤(1)所合成产物用乙醇与丙酮洗涤,随后离心分离出固态产物;(2) washing the product synthesized in step (1) with ethanol and acetone, and then centrifuging to separate the solid product;
(3)将步骤(2)所合成样品在干燥箱中干燥12h,得到铂镍纳米晶修饰碳基催化剂PtNi/C(记为:合成PtNi/C-200℃-Pt∶Ni=1∶3)。铂镍纳米晶修饰碳基催化剂PtNi/C的组成如表1所示。(3) The sample synthesized in step (2) was dried in a drying oven for 12 hours to obtain a platinum-nickel nanocrystal modified carbon-based catalyst PtNi/C (recorded as: synthesized PtNi/C-200°C-Pt:Ni=1:3). The composition of the platinum-nickel nanocrystal modified carbon-based catalyst PtNi/C is shown in Table 1.
表1实施例7-11中制备的铂镍纳米晶修饰碳基催化剂的组成Table 1 Composition of the platinum-nickel nanocrystal-modified carbon-based catalyst prepared in Examples 7-11
图6是本发明实施例7-11中不同铂镍比例所合成PtNi/C催化剂在碱性溶液(0.1M氢氧化钾)中氧还原反应性能测试的结果。通过对比发现,在铂镍比例从3∶1增加到1∶2时,随着合成样品时铂镍比例的增加,催化氧还原反应性能测试的结果越好,在铂镍比例升高到1∶3时,合成样品时铂镍比例对氧还原反应性能相对于1∶2时所合成PtNi/C催化剂略差。因此,铂镍比例为1∶2时所合成的PtNi/C催化剂为合成样品的最优铂镍配比。Figure 6 is the result of the oxygen reduction reaction performance test of the PtNi/C catalyst synthesized by different platinum-nickel ratios in Examples 7-11 of the present invention in an alkaline solution (0.1M potassium hydroxide). By comparison, it was found that when the platinum-nickel ratio increased from 3:1 to 1:2, as the platinum-nickel ratio increased during the synthesis of the sample, the result of the catalytic oxygen reduction reaction performance test was better. When the platinum-nickel ratio increased to 1:3, the platinum-nickel ratio during the synthesis of the sample had a slightly worse oxygen reduction reaction performance than the PtNi/C catalyst synthesized at 1:2. Therefore, the PtNi/C catalyst synthesized at a platinum-nickel ratio of 1:2 is the optimal platinum-nickel ratio for the synthetic sample.
对比例1Comparative Example 1
采用商业Pt/C-5%、商业Pt/C-20%进行氧还原反应性能测试;Commercial Pt/C-5% and commercial Pt/C-20% were used to test the oxygen reduction reaction performance;
图7是本发明实施例10中的PtNi/C-200℃-Pt∶Ni=1∶2、对比例1中商业Pt/C-5%、商业Pt/C-20%的氧还原反应性能测试图。7 is a test graph of the oxygen reduction reaction performance of PtNi/C-200°C-Pt∶Ni=1∶2 in Example 10 of the present invention, commercial Pt/C-5% and commercial Pt/C-20% in Comparative Example 1.
对比例2Comparative Example 2
方法同实施例10,不同之处在于未使用稳定剂苯甲酸;图8是本对比例2制备的催化剂的透射电子显微图。The method is the same as Example 10, except that the stabilizer benzoic acid is not used; FIG8 is a transmission electron micrograph of the catalyst prepared in this comparative example 2.
对比例3Comparative Example 3
方法同实施例10,不同之处在于未使用结构导向剂十六烷基三甲基溴化铵;图9是本对比例3制备的催化剂的透射电子显微图。The method is the same as Example 10, except that the structure directing agent hexadecyltrimethylammonium bromide is not used; FIG. 9 is a transmission electron micrograph of the catalyst prepared in this comparative example 3.
对比例4Comparative Example 4
方法同实施例10,不同之处在于未使用稳定剂苯甲酸及结构导向剂十六烷基三甲基溴化铵;图10是本对比例4制备的催化剂的透射电子显微图;图11是本对比例2-4中制备的催化剂的氧还原反应性能测试图。The method is the same as Example 10, except that the stabilizer benzoic acid and the structure-directing agent hexadecyltrimethylammonium bromide are not used; Figure 10 is a transmission electron micrograph of the catalyst prepared in this comparative example 4; Figure 11 is a test graph of the oxygen reduction reaction performance of the catalyst prepared in this comparative example 2-4.
此外,本案发明人还参照前述实施例,以本说明书述及的其它原料、工艺操作、工艺条件进行了试验,并均获得了较为理想的结果。In addition, the inventors of this case also referred to the aforementioned embodiments and conducted experiments with other raw materials, process operations, and process conditions described in this specification, and obtained relatively ideal results.
应当理解,本发明的技术方案不限于上述具体实施案例的限制,凡是在不脱离本发明宗旨和权利要求所保护的范围情况下,根据本发明的技术方案做出的技术变形,均落于本发明的保护范围之内。It should be understood that the technical solution of the present invention is not limited to the above-mentioned specific implementation cases. Any technical deformation made according to the technical solution of the present invention without departing from the scope of protection of the purpose of the present invention and the claims shall fall within the protection scope of the present invention.
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