CN105576263A - High-performance fuel cell catalyst and preparation method thereof - Google Patents
High-performance fuel cell catalyst and preparation method thereof Download PDFInfo
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- 239000003054 catalyst Substances 0.000 title claims abstract description 79
- 239000000446 fuel Substances 0.000 title claims abstract description 45
- 238000002360 preparation method Methods 0.000 title claims abstract description 14
- 239000002082 metal nanoparticle Substances 0.000 claims abstract description 39
- 229910052751 metal Inorganic materials 0.000 claims abstract description 19
- 239000002184 metal Substances 0.000 claims abstract description 19
- 229910044991 metal oxide Inorganic materials 0.000 claims abstract description 18
- 150000004706 metal oxides Chemical class 0.000 claims abstract description 18
- 238000000034 method Methods 0.000 claims abstract description 12
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 claims description 70
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 claims description 38
- 229910052697 platinum Inorganic materials 0.000 claims description 32
- 238000003756 stirring Methods 0.000 claims description 30
- 239000002105 nanoparticle Substances 0.000 claims description 28
- 150000003839 salts Chemical class 0.000 claims description 27
- 239000010931 gold Substances 0.000 claims description 26
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 claims description 25
- 229910052737 gold Inorganic materials 0.000 claims description 25
- 229910052720 vanadium Inorganic materials 0.000 claims description 25
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 21
- LEONUFNNVUYDNQ-UHFFFAOYSA-N vanadium atom Chemical compound [V] LEONUFNNVUYDNQ-UHFFFAOYSA-N 0.000 claims description 19
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 claims description 18
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 claims description 18
- 229910052750 molybdenum Inorganic materials 0.000 claims description 18
- 239000011733 molybdenum Substances 0.000 claims description 18
- 229910052758 niobium Inorganic materials 0.000 claims description 18
- 239000010955 niobium Substances 0.000 claims description 18
- GUCVJGMIXFAOAE-UHFFFAOYSA-N niobium atom Chemical compound [Nb] GUCVJGMIXFAOAE-UHFFFAOYSA-N 0.000 claims description 18
- 229910052763 palladium Inorganic materials 0.000 claims description 18
- 229910052799 carbon Inorganic materials 0.000 claims description 17
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 claims description 17
- 229910052721 tungsten Inorganic materials 0.000 claims description 17
- 239000010937 tungsten Substances 0.000 claims description 17
- 239000000126 substance Substances 0.000 claims description 16
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 14
- KJTLSVCANCCWHF-UHFFFAOYSA-N Ruthenium Chemical compound [Ru] KJTLSVCANCCWHF-UHFFFAOYSA-N 0.000 claims description 14
- 229910052802 copper Inorganic materials 0.000 claims description 14
- 239000010949 copper Substances 0.000 claims description 14
- 239000011258 core-shell material Substances 0.000 claims description 14
- 229910052707 ruthenium Inorganic materials 0.000 claims description 14
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 12
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 9
- 239000008367 deionised water Substances 0.000 claims description 9
- 229910021641 deionized water Inorganic materials 0.000 claims description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 9
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 8
- 229910001092 metal group alloy Inorganic materials 0.000 claims description 8
- 239000002539 nanocarrier Substances 0.000 claims description 8
- 239000003153 chemical reaction reagent Substances 0.000 claims description 7
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims description 6
- 229910017052 cobalt Inorganic materials 0.000 claims description 6
- 239000010941 cobalt Substances 0.000 claims description 6
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 claims description 6
- 229910052759 nickel Inorganic materials 0.000 claims description 6
- 239000006229 carbon black Substances 0.000 claims description 5
- 238000006073 displacement reaction Methods 0.000 claims description 5
- 239000002245 particle Substances 0.000 claims description 5
- 239000013078 crystal Substances 0.000 claims description 4
- 238000000151 deposition Methods 0.000 claims description 4
- 230000008021 deposition Effects 0.000 claims description 4
- 229910052742 iron Inorganic materials 0.000 claims description 4
- 150000003057 platinum Chemical class 0.000 claims description 4
- 238000004758 underpotential deposition Methods 0.000 claims description 4
- XHCLAFWTIXFWPH-UHFFFAOYSA-N [O-2].[O-2].[O-2].[O-2].[O-2].[V+5].[V+5] Chemical compound [O-2].[O-2].[O-2].[O-2].[O-2].[V+5].[V+5] XHCLAFWTIXFWPH-UHFFFAOYSA-N 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 3
- 229910001935 vanadium oxide Inorganic materials 0.000 claims description 3
- WGLPBDUCMAPZCE-UHFFFAOYSA-N Trioxochromium Chemical compound O=[Cr](=O)=O WGLPBDUCMAPZCE-UHFFFAOYSA-N 0.000 claims description 2
- 229910045601 alloy Inorganic materials 0.000 claims description 2
- 239000000956 alloy Substances 0.000 claims description 2
- 239000002134 carbon nanofiber Substances 0.000 claims description 2
- 239000002041 carbon nanotube Substances 0.000 claims description 2
- 229910021393 carbon nanotube Inorganic materials 0.000 claims description 2
- 229910000423 chromium oxide Inorganic materials 0.000 claims description 2
- 229910021389 graphene Inorganic materials 0.000 claims description 2
- 150000002739 metals Chemical group 0.000 claims description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 2
- 229910000476 molybdenum oxide Inorganic materials 0.000 claims description 2
- 229910000484 niobium oxide Inorganic materials 0.000 claims description 2
- URLJKFSTXLNXLG-UHFFFAOYSA-N niobium(5+);oxygen(2-) Chemical compound [O-2].[O-2].[O-2].[O-2].[O-2].[Nb+5].[Nb+5] URLJKFSTXLNXLG-UHFFFAOYSA-N 0.000 claims description 2
- QGLKJKCYBOYXKC-UHFFFAOYSA-N nonaoxidotritungsten Chemical compound O=[W]1(=O)O[W](=O)(=O)O[W](=O)(=O)O1 QGLKJKCYBOYXKC-UHFFFAOYSA-N 0.000 claims description 2
- PQQKPALAQIIWST-UHFFFAOYSA-N oxomolybdenum Chemical compound [Mo]=O PQQKPALAQIIWST-UHFFFAOYSA-N 0.000 claims description 2
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 claims description 2
- 229910001930 tungsten oxide Inorganic materials 0.000 claims description 2
- 239000000463 material Substances 0.000 claims 15
- CEYULKASIQJZGP-UHFFFAOYSA-L disodium;2-(carboxymethyl)-2-hydroxybutanedioate Chemical compound [Na+].[Na+].[O-]C(=O)CC(O)(C(=O)O)CC([O-])=O CEYULKASIQJZGP-UHFFFAOYSA-L 0.000 claims 6
- 238000005406 washing Methods 0.000 claims 3
- 239000012467 final product Substances 0.000 claims 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 22
- 229910052760 oxygen Inorganic materials 0.000 abstract description 22
- 239000001301 oxygen Substances 0.000 abstract description 22
- 238000006722 reduction reaction Methods 0.000 abstract description 20
- 230000000694 effects Effects 0.000 abstract description 11
- 239000003792 electrolyte Substances 0.000 abstract description 4
- 239000012528 membrane Substances 0.000 abstract description 4
- 239000007788 liquid Substances 0.000 description 27
- 239000010936 titanium Substances 0.000 description 18
- 229910052719 titanium Inorganic materials 0.000 description 18
- -1 titanium dioxide-modified gold Chemical class 0.000 description 12
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 11
- 238000010586 diagram Methods 0.000 description 11
- 229910052804 chromium Inorganic materials 0.000 description 9
- 239000011651 chromium Substances 0.000 description 9
- NLJMYIDDQXHKNR-UHFFFAOYSA-K sodium citrate Chemical compound O.O.[Na+].[Na+].[Na+].[O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O NLJMYIDDQXHKNR-UHFFFAOYSA-K 0.000 description 9
- 239000001509 sodium citrate Substances 0.000 description 9
- 125000004429 atom Chemical group 0.000 description 8
- 239000003638 chemical reducing agent Substances 0.000 description 6
- 239000010410 layer Substances 0.000 description 6
- 239000002356 single layer Substances 0.000 description 6
- 238000002525 ultrasonication Methods 0.000 description 6
- 238000001179 sorption measurement Methods 0.000 description 5
- 230000009257 reactivity Effects 0.000 description 4
- VXUYXOFXAQZZMF-UHFFFAOYSA-N titanium(IV) isopropoxide Chemical compound CC(C)O[Ti](OC(C)C)(OC(C)C)OC(C)C VXUYXOFXAQZZMF-UHFFFAOYSA-N 0.000 description 4
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 3
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 3
- 238000005430 electron energy loss spectroscopy Methods 0.000 description 3
- 229910052744 lithium Inorganic materials 0.000 description 3
- 229910052708 sodium Inorganic materials 0.000 description 3
- 239000011734 sodium Substances 0.000 description 3
- 230000005540 biological transmission Effects 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000007806 chemical reaction intermediate Substances 0.000 description 2
- 125000004430 oxygen atom Chemical group O* 0.000 description 2
- 239000004408 titanium dioxide Substances 0.000 description 2
- 238000003775 Density Functional Theory Methods 0.000 description 1
- 229910021549 Vanadium(II) chloride Inorganic materials 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 238000004364 calculation method Methods 0.000 description 1
- 231100000481 chemical toxicant Toxicity 0.000 description 1
- 230000003749 cleanliness Effects 0.000 description 1
- 230000002860 competitive effect Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 150000002343 gold Chemical class 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000011943 nanocatalyst Substances 0.000 description 1
- MUMZUERVLWJKNR-UHFFFAOYSA-N oxoplatinum Chemical compound [Pt]=O MUMZUERVLWJKNR-UHFFFAOYSA-N 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 229920005597 polymer membrane Polymers 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- CCEKAJIANROZEO-UHFFFAOYSA-N sulfluramid Chemical group CCNS(=O)(=O)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)F CCEKAJIANROZEO-UHFFFAOYSA-N 0.000 description 1
- 150000003608 titanium Chemical class 0.000 description 1
- 239000003440 toxic substance Substances 0.000 description 1
- 238000002604 ultrasonography Methods 0.000 description 1
- ITAKKORXEUJTBC-UHFFFAOYSA-L vanadium(ii) chloride Chemical compound Cl[V]Cl ITAKKORXEUJTBC-UHFFFAOYSA-L 0.000 description 1
Classifications
-
- 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
-
- 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
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Catalysts (AREA)
Abstract
Description
技术领域technical field
本发明属燃料电池催化剂领域,尤其涉及一种高性能燃料电池催化剂及其制备方法。The invention belongs to the field of fuel cell catalysts, in particular to a high-performance fuel cell catalyst and a preparation method thereof.
背景技术Background technique
能源与社会进步、国民经济的发展有着密切联系,人类社会前进的每一步都与能源的开发利用息息相关。人类对能源利用的每一次重大突破都伴随着科技的进步,从而促进生产力的发展。随着经济增长,技术进步,以及人口的猛增,人类社会对能源的需求量与日俱增。随着化石能源的日趋枯竭和环境污染问题的日益严重,如果找不到有效的替代能源,人类社会将面临全面的能源危机。燃料电池作为一种直接将化学能转化为电能的发电装置,因为其高效性、环境友好性,被认为是21世纪首选的洁净能源技术。电解质膜燃料电池因其高效、清洁、低温等优点,被认为是最有前途、最有竞争力、最有可能实现产业化应用的燃料电池[R.Borup,etal.,Chem.Rev.107(2007)3904;R.Dillon,etal.,J.PowerSources127(2004)112]。电极作为燃料电池的关键部件,其电催化性能的优劣直接影响燃料电池的整体性能。电解质膜燃料电池低的阴极氧还原反应速率是制约电解质膜燃料电池商业化的关键因素[H.A.Gasteiger,etal.,Science324(2009)48;M.K.Debe,Nature486(2012)43;V.R.Stamenkovic,etal.,Science315(2007)493]。铂(Pt)基催化剂由于其高活性和高稳定性,是当前最好的聚合物燃料电池电极催化剂,被广泛用于燃料电池的阴、阳两极[C.Chen,etal.,Science343(2014)1339;L.Zhang,etal.,Science349(2015)412]。然而,由于Pt资源匮乏,价格昂贵,并且相对于聚合物膜燃料电池阳极,阴极的氧还原反应速率低决定了需要在阴极加大Pt的用量,大大增加了燃料电池的成本。因此,开发新型高性能燃料电池催化剂成为燃料电池主要研究方向之一,具有重要的应用价值和科学意义。Energy is closely related to social progress and the development of the national economy, and every step forward in human society is closely related to the development and utilization of energy. Every major breakthrough in human energy utilization is accompanied by scientific and technological progress, thereby promoting the development of productivity. With economic growth, technological progress, and population growth, the demand for energy in human society is increasing day by day. With the depletion of fossil energy and the seriousness of environmental pollution, if no effective alternative energy is found, human society will face a comprehensive energy crisis. As a power generation device that directly converts chemical energy into electrical energy, fuel cells are considered to be the preferred clean energy technology in the 21st century because of their high efficiency and environmental friendliness. Electrolyte membrane fuel cells are considered to be the most promising, most competitive, and most likely to achieve industrial applications due to their advantages of high efficiency, cleanliness, and low temperature [R.Borup, et al., Chem.Rev.107( 2007) 3904; R. Dillon, et al., J. Power Sources 127 (2004) 112]. As a key component of the fuel cell, the electrocatalytic performance of the electrode directly affects the overall performance of the fuel cell. The low cathode oxygen reduction reaction rate of electrolyte membrane fuel cells is a key factor restricting the commercialization of electrolyte membrane fuel cells [H.A.Gasteiger, et al., Science324(2009)48; M.K.Debe, Nature486(2012)43; Science 315 (2007) 493]. Platinum (Pt)-based catalysts are currently the best polymer fuel cell electrode catalysts due to their high activity and high stability, and are widely used in the cathode and anode of fuel cells [C. Chen, et al., Science343 (2014) 1339; L. Zhang, et al., Science 349 (2015) 412]. However, due to the scarcity and high price of Pt resources, and the low oxygen reduction reaction rate of the cathode compared with the anode of the polymer membrane fuel cell, it is necessary to increase the amount of Pt in the cathode, which greatly increases the cost of the fuel cell. Therefore, the development of new high-performance fuel cell catalysts has become one of the main research directions of fuel cells, which has important application value and scientific significance.
新型燃料电池催化剂的开发可以从两方面入手:一是提高催化剂的反应活性和稳定性;二是在减少Pt用量的同时保持催化剂较高的反应活性,即提高Pt的利用效率。燃料电池阴、阳两极的电催化反应活性随催化剂表面金属原子与反应中间物吸附强度的变化而变化,且遵循火山图变化规律。以氧还原反应为例,催化剂的氧还原反应活性随着表面金属原子与氧的吸附强度的增加而先增加后降低[J.Greeley,etal.,Nat.Chem.1(2009)552]。所以提高催化剂的反应活性可以通过改变催化剂表面金属原子与反应中间物的吸附强度来实现。密度泛函理论计算结果表明,铂-氧(Pt-O)键键能降低0.2eV可使氧还原反应活性达到最高,而且,对于Pt纳米粒子而言,位于平整晶面上的Pt-O键键能小于位于顶角和棱上的Pt-O键键能[J.Greeley,etal.,Nat.Chem.1(2009)552]。可见,设计一种新型的燃料电池催化剂结构,使Pt原子位于催化剂纳米粒子表面的平整晶面上,获得较低的Pt-O键键能,使金属氧化物位于纳米催化剂粒子表面的棱和顶角上,金属氧化物中的氧原子与吸附在Pt表面的氧原子之间发生排斥作用,可进一步减小Pt表面氧的吸附强度,是提高催化剂氧还原反应活性的有效、可行的方法。The development of new fuel cell catalysts can start from two aspects: one is to improve the reactivity and stability of the catalyst; the other is to reduce the amount of Pt while maintaining a high reactivity of the catalyst, that is, to increase the utilization efficiency of Pt. The electrocatalytic reactivity of the cathode and anode of the fuel cell varies with the adsorption strength of the metal atoms on the catalyst surface and the reaction intermediates, and follows the variation law of the volcano diagram. Taking the oxygen reduction reaction as an example, the oxygen reduction reaction activity of the catalyst first increases and then decreases with the increase of the adsorption strength of surface metal atoms and oxygen [J.Greeley, et al., Nat.Chem.1(2009)552]. Therefore, improving the reactivity of the catalyst can be achieved by changing the adsorption strength between the metal atoms on the catalyst surface and the reaction intermediates. Density functional theory calculation results show that the reduction of platinum-oxygen (Pt-O) bond energy by 0.2eV can lead to the highest oxygen reduction reaction activity, and, for Pt nanoparticles, the Pt-O bond on the flat crystal plane The bond energy is smaller than that of Pt-O bonds located on the corners and edges [J. Greeley, et al., Nat. Chem. 1 (2009) 552]. It can be seen that designing a new type of fuel cell catalyst structure allows Pt atoms to be located on the flat crystal plane of the surface of the catalyst nanoparticle to obtain a lower Pt-O bond energy, so that the metal oxide is located on the edge and top of the surface of the nanocatalyst particle. On the corner, the repulsion between the oxygen atoms in the metal oxide and the oxygen atoms adsorbed on the Pt surface can further reduce the adsorption strength of oxygen on the Pt surface, which is an effective and feasible method to improve the oxygen reduction reaction activity of the catalyst.
发明内容Contents of the invention
本发明的目的是提出一种成本较低、耐碱性与耐酸性能更好的一种高性能燃料电池催化剂。The purpose of the invention is to propose a high-performance fuel cell catalyst with lower cost and better alkali resistance and acid resistance.
为了实现上述目的本发明采用如下技术方案:In order to achieve the above object, the present invention adopts the following technical solutions:
一种高性能燃料电池催化剂,其特征在于:由金属和金属氧化物构成;金属形成表面具有晶面、棱和顶角的金属纳米粒子;金属氧化物位于金属纳米粒子表面的棱和顶角上。A high-performance fuel cell catalyst, characterized in that: it is composed of metal and metal oxide; the metal forms metal nanoparticles with crystal planes, edges and vertex angles on the surface; the metal oxide is located on the edges and vertex angles on the surface of the metal nanoparticles .
所述的一种高性能燃料电池催化剂,其特征在于:所述的金属纳米粒子是单金属纳米粒子,或多种金属形式的合金纳米粒子,或具有核-壳结构的金属纳米粒子;所述的金属纳米粒子粒径小于50nm。The above-mentioned high-performance fuel cell catalyst is characterized in that: the metal nanoparticles are single metal nanoparticles, or alloy nanoparticles in the form of multiple metals, or metal nanoparticles with a core-shell structure; The particle size of metal nanoparticles is less than 50nm.
所述的一种高性能燃料电池催化剂,其特征在于,所述的金属氧化物选自氧化钛、氧化钒、氧化钨、氧化钼、氧化铌、氧化铬中的一种或多种的混合。The above high-performance fuel cell catalyst is characterized in that the metal oxide is selected from one or more of titanium oxide, vanadium oxide, tungsten oxide, molybdenum oxide, niobium oxide, and chromium oxide.
所述的一种高性能燃料电池催化剂,其特征在于,所述的金属纳米粒子是单金属纳米粒子时,单金属指的是铂、钯、金中的一种;当所述的金属纳米粒子是金属合金纳米粒子时,金属合金指的是含金、钯、铜、镍、钴、钌、铁中的两种或多种;当所述的金属纳米粒子是具有核-壳结构的金属纳米粒子时,核-壳型金属中的核金属指的是金、钯或钌的一种或多种混合。Described a kind of high-performance fuel cell catalyst is characterized in that, when described metal nanoparticle is single metal nanoparticle, single metal refers to a kind of in platinum, palladium, gold; When described metal nanoparticle When it is a metal alloy nanoparticle, the metal alloy refers to two or more of gold, palladium, copper, nickel, cobalt, ruthenium, and iron; when the metal nanoparticle is a metal nanoparticle with a core-shell structure In the case of particles, the core metal in the core-shell metal refers to one or more mixtures of gold, palladium or ruthenium.
所述的高性能燃料电池催化剂的制备方法,其特征在于:当所述的金属纳米粒子是单金属纳米粒子时,其具体步骤如下:The preparation method of the high-performance fuel cell catalyst is characterized in that: when the metal nanoparticles are single metal nanoparticles, the specific steps are as follows:
(1)称取碳纳米载体置于无水乙醇中,制成碳浓度为1-5g/ml的混合液体,超声或搅拌10-60min;(1) Weigh the carbon nanocarrier and place it in absolute ethanol to make a mixed liquid with a carbon concentration of 1-5g/ml, sonicate or stir for 10-60min;
(2)在混合液体中加入柠檬酸钠,所加入的柠檬酸钠的质量是碳质量的0.5-5倍,超声或搅拌10-60min;(2) Add sodium citrate to the mixed liquid, the mass of the added sodium citrate is 0.5-5 times of the carbon mass, sonicate or stir for 10-60min;
(3)在混合液体中加入含钛、钒、钨、钼、铌、铬元素的盐类中的一种或多种混合,超声或搅拌10-60min;(3) Add one or more of the salts containing titanium, vanadium, tungsten, molybdenum, niobium, and chromium elements into the mixed liquid, and then ultrasonically or stir for 10-60 minutes;
(4)在混合液体中加入还原试剂,所加入的还原试剂的物质的量为含钛、钒、钨、钼、铌、铬元素的盐类物质的总量的1.5-20倍,超声或搅拌10-120min;(4) Add a reducing agent to the mixed liquid. The amount of the added reducing agent is 1.5-20 times the total amount of the salt substances containing titanium, vanadium, tungsten, molybdenum, niobium, and chromium. Ultrasonic or stirring 10-120min;
(5)在混合液体中加入一种含铂或钯元素的盐类,所加入的含铂、金或钯元素的盐类物质的量为含钛、钒、钨、钼、铌、铬元素的盐类物质的量总和的0.1-3倍,超声或搅拌10-60min;(5) A salt containing platinum or palladium is added to the mixed liquid, and the amount of the salt containing platinum, gold or palladium added is that of titanium, vanadium, tungsten, molybdenum, niobium, and chromium 0.1-3 times the sum of the amount of salt substances, ultrasonic or stirring for 10-60min;
(6)离心、过滤、去离子水洗涤、干燥,制得金属氧化物修饰的单金属纳米粒子催化剂,即得;(6) Centrifuge, filter, wash with deionized water, and dry to prepare a metal oxide-modified single-metal nanoparticle catalyst;
所述的高性能燃料电池催化剂的制备方法,其特征在于:当所述的金属纳米粒子是金属合金纳米粒子时,其具体步骤如下:The preparation method of the high-performance fuel cell catalyst is characterized in that: when the metal nanoparticles are metal alloy nanoparticles, the specific steps are as follows:
(1)称取碳纳米载体置于无水乙醇中,制成碳浓度为1-5g/ml的混合液体,超声或搅拌10-60min;(1) Weigh the carbon nanocarrier and place it in absolute ethanol to make a mixed liquid with a carbon concentration of 1-5g/ml, sonicate or stir for 10-60min;
(2)在混合液体中加入柠檬酸钠,所加入的柠檬酸钠的质量是碳质量的0.5-5倍,超声或搅拌10-60min;(2) Add sodium citrate to the mixed liquid, the mass of the added sodium citrate is 0.5-5 times of the carbon mass, sonicate or stir for 10-60min;
(3)在混合液体中加入含钛、钒、钨、钼、铌、铬元素的盐类中的一种或多种混合,超声或搅拌10-60min;(3) Add one or more of the salts containing titanium, vanadium, tungsten, molybdenum, niobium, and chromium elements into the mixed liquid, and then ultrasonically or stir for 10-60 minutes;
(4)在混合液体中加入还原试剂,所加入的还原试剂的物质的量为含钛、钒、钨、钼、铌、铬元素的盐类物质的总量的1.5-20倍,超声或搅拌10-120min;(4) Add a reducing agent to the mixed liquid. The amount of the added reducing agent is 1.5-20 times the total amount of the salt substances containing titanium, vanadium, tungsten, molybdenum, niobium, and chromium. Ultrasonic or stirring 10-120min;
(5)在混合液体中加入含铂元素的盐类与含金、钯、铜、镍、钴、钌、铁元素的盐类两种或多种混合,所加入的含铂、金、钯、铜、镍、钴、钌、铁元素的盐类物质的量总和为含钛、钒、钨、钼、铌、铬元素的盐类物质的量总和的0.1-3倍,超声或搅拌10-60min;(5) Add platinum-containing salts and two or more salts containing gold, palladium, copper, nickel, cobalt, ruthenium, and iron elements into the mixed liquid, and the added salts containing platinum, gold, palladium, The sum of the salts of copper, nickel, cobalt, ruthenium and iron is 0.1-3 times the sum of the salts of titanium, vanadium, tungsten, molybdenum, niobium and chromium, ultrasonic or stirring for 10-60min ;
(6)离心、过滤、去离子水洗涤、干燥,制得金属氧化物修饰的金属合金纳米粒子催化剂;(6) Centrifuge, filter, wash with deionized water, and dry to prepare a metal alloy nanoparticle catalyst modified by metal oxide;
所述的高性能燃料电池催化剂的制备方法,其特征在于:当所述的金属纳米粒子是具有核-壳结构的金属纳米粒子时,其具体步骤如下:The preparation method of the high-performance fuel cell catalyst is characterized in that: when the metal nanoparticles are metal nanoparticles with a core-shell structure, the specific steps are as follows:
(1)称取碳纳米载体置于无水乙醇中,制成碳浓度为1-5g/ml的混合液体,超声或搅拌10-60min;(1) Weigh the carbon nanocarrier and place it in absolute ethanol to make a mixed liquid with a carbon concentration of 1-5g/ml, sonicate or stir for 10-60min;
(2)在混合液体中加入柠檬酸钠,所加入的柠檬酸钠的质量是碳质量的0.5-5倍,超声或搅拌10-60min;(2) Add sodium citrate to the mixed liquid, the mass of the added sodium citrate is 0.5-5 times of the carbon mass, sonicate or stir for 10-60min;
(3)在混合液体中加入含钛、钒、钨、钼、铌、铬元素的盐类中的一种或多种混合,超声或搅拌10-60min;(3) Add one or more of the salts containing titanium, vanadium, tungsten, molybdenum, niobium, and chromium elements into the mixed liquid, and then ultrasonically or stir for 10-60 minutes;
(4)在混合液体中加入还原试剂,所加入的还原试剂的物质的量为含钛、钒、钨、钼、铌、铬元素的盐类物质的量的1.5-20倍,超声或搅拌10-120min;(4) Add a reducing agent to the mixed liquid. The amount of the added reducing agent is 1.5-20 times the amount of the salt containing titanium, vanadium, tungsten, molybdenum, niobium, and chromium. Ultrasound or stir for 10 -120min;
(5)在混合液体中加入含金、钯或钌元素的盐类一种或多种混合,所加入的含金、钯、钌元素的盐类物质的量总和为含钛、钒、钨、钼、铌、铬元素的盐类物质的量总和的0.1-3倍,超声或搅拌10-60min;(5) Add one or more salts containing gold, palladium, or ruthenium to the mixed liquid, and the total amount of salts containing gold, palladium, and ruthenium added is 0.1-3 times the sum of the salts of molybdenum, niobium, and chromium, ultrasonic or stirring for 10-60 minutes;
(6)离心、过滤、去离子水洗涤、干燥;(6) Centrifuge, filter, wash with deionized water, and dry;
(7)采用欠电位沉积方法在步骤(6)所制得的金属纳米粒子表面沉积单层铜,在金属氧化物表面不发生沉积,再将其置于含有铂盐的溶液中发生置换反应,使铜被铂置换形成单层铂,或重复步骤(7)数次以实现在金、钯或钌纳米粒子表面沉积多层铂,即制得金属氧化物修饰的核-壳结构金属纳米粒子催化剂。(7) Deposit a single layer of copper on the surface of the metal nanoparticles prepared in step (6) by using the underpotential deposition method, and no deposition occurs on the surface of the metal oxide, and then place it in a solution containing a platinum salt to undergo a displacement reaction, Replace copper with platinum to form a single layer of platinum, or repeat step (7) several times to deposit multiple layers of platinum on the surface of gold, palladium or ruthenium nanoparticles, that is, to obtain a metal oxide-modified core-shell structure metal nanoparticle catalyst .
所述的高性能燃料电池催化剂的制备方法,其特征在于:所述的碳纳米载体选自碳黑、碳纳米管、碳纳米纤维、石墨烯等中的一种或多种混合。The preparation method of the high-performance fuel cell catalyst is characterized in that: the carbon nanocarrier is selected from one or more mixtures of carbon black, carbon nanotubes, carbon nanofibers, graphene and the like.
本发明的有益效果:Beneficial effects of the present invention:
本发明用简单的制备方法实现了对催化剂表面结构原子级别的调控,使催化剂的氧还原反应性能大幅提高。The invention uses a simple preparation method to realize the atomic level regulation of the surface structure of the catalyst, so that the oxygen reduction reaction performance of the catalyst is greatly improved.
本发明所述的新型结构燃料电池催化剂制备方法简单,操作方便,常温下进行,无需依靠大型的、特殊的装置和器械来实现,容易实现批量化生产,且不使用有毒的化学试剂,不污染环境。The preparation method of the fuel cell catalyst with a new structure described in the present invention is simple, easy to operate, and can be carried out at normal temperature without relying on large-scale and special devices and equipment, and it is easy to realize mass production without using toxic chemical reagents and causing no pollution. environment.
本发明制得的新型结构燃料电池催化剂,由于有效降低了Pt表面的氧吸附强度,使催化剂的氧还原反应活性大幅提高。同时,金属氧化物位于具有较低配位数的棱和顶角位置,能够有效减小内层金属原子溢出,不仅可以较好地保护内层原子减小其受到腐蚀,而且还可以降低因内层金属原子溢出而造成的对Pt活性位点的阻塞,从而提高催化剂的稳定性。The fuel cell catalyst with a novel structure prepared by the invention greatly improves the oxygen reduction reaction activity of the catalyst because the oxygen adsorption strength on the Pt surface is effectively reduced. At the same time, the metal oxide is located at the edge and vertex with a lower coordination number, which can effectively reduce the overflow of the inner layer metal atoms, not only can better protect the inner layer atoms from corrosion, but also reduce the inner layer atoms. The blocking of Pt active sites caused by the overflow of layer metal atoms improves the stability of the catalyst.
本发明制得的新型结构燃料电池催化剂,其中,金属氧化物修饰的核-壳结构金属纳米粒子催化剂在有效提高催化剂活性和稳定性的同时,还大大降低了Pt的用量,是一种性能非常优越、极易实现商品化应用的燃料电池催化剂。The novel structure fuel cell catalyst prepared by the present invention, wherein the metal oxide-modified core-shell structure metal nanoparticle catalyst can effectively improve the catalyst activity and stability while greatly reducing the amount of Pt, is a very performance A fuel cell catalyst that is superior and extremely easy to realize commercial application.
附图说明Description of drawings
图1新型结构金属氧化物修饰的核-壳结构金属纳米粒子催化剂结构示意图。Fig. 1 Schematic diagram of the structure of the core-shell metal nanoparticle catalyst modified by the novel structure metal oxide.
图2二氧化钛修饰金纳米粒子扫描透射显微镜-电子能量损失谱元素面扫描图。Fig. 2 Scanning transmission microscope-electron energy loss spectroscopy element surface scanning diagram of titanium dioxide-modified gold nanoparticles.
图3二氧化钛修饰AuPt核-壳结构金属纳米粒子催化剂与商品化Pt催化剂的氧还原性能比较示意图。Fig. 3 Schematic diagram comparing the oxygen reduction performance of titania-modified AuPt core-shell metal nanoparticle catalysts and commercial Pt catalysts.
图4二氧化钛修饰AuPt核-壳结构金属纳米粒子催化剂的稳定性示意图。Fig. 4 Schematic diagram of the stability of titanium dioxide-modified AuPt core-shell metal nanoparticle catalysts.
图5氧化钒修饰AuPt核-壳结构金属纳米粒子催化剂与商品化Pt催化剂的氧还原性能比较示意图。Fig. 5 Schematic diagram comparing the oxygen reduction performance of vanadium oxide-modified AuPt core-shell metal nanoparticle catalysts and commercial Pt catalysts.
图6氧化钒修饰AuPt核-壳结构金属纳米粒子催化剂的稳定性示意图。Figure 6 Schematic diagram of the stability of vanadium oxide-modified AuPt core-shell metal nanoparticle catalysts.
具体实施方式detailed description
实施例1:Example 1:
称取碳黑140g置于50ml无水乙醇中,超声60min后在混合液体中加入柠檬酸钠300mg,超声30min。然后在混合液体中加入0.9mmol的异丙氧基钛,超声30min。继续在混合液体中加入2ml1mol/L的三乙基氢化硼锂,超声反应30min后加入0.1mmol的氯金酸钠,超声60min。将混合液体离心、过滤、去离子水洗涤后置于真空烘箱中干燥。图1为二氧化钛修饰Au纳米粒子的扫描透射显微镜-电子能量损失谱(STEM-EELS)元素含量面扫描图,从图1可以看出本方法制得的二氧化钛修饰金纳米粒子中钛分布于金纳米粒子的表面,且集中于金纳米粒子的棱和顶角位置。Weigh 140g of carbon black and place it in 50ml of absolute ethanol, after ultrasonication for 60min, add 300mg of sodium citrate to the mixed liquid, and ultrasonication for 30min. Then, 0.9 mmol of titanium isopropoxide was added to the mixed liquid and ultrasonicated for 30 min. Continue to add 2ml of 1mol/L lithium triethyl borohydride to the mixed liquid, and then add 0.1mmol of sodium chloroaurate after ultrasonic reaction for 30 minutes, and ultrasonic for 60 minutes. The mixed liquid was centrifuged, filtered, washed with deionized water, and then dried in a vacuum oven. Figure 1 is a scanning transmission microscope-electron energy loss spectroscopy (STEM-EELS) element content surface scan diagram of titanium dioxide-modified Au nanoparticles. It can be seen from Figure 1 that titanium is distributed in gold nanoparticles in titanium dioxide-modified gold nanoparticles prepared by this method. The surface of the particle, and concentrated on the edges and corners of the gold nanoparticles.
实施例2:Example 2:
称取碳黑140g置于50ml无水乙醇中,超声60min后在混合液体中加入柠檬酸钠300mg,超声30min。然后在混合液体中加入0.3mmol的异丙氧基钛,超声30min。继续在混合液体中加入2ml1mol/L的三乙基氢化硼锂,反应30min后加入0.1mmol的氯金酸钠,超声60min。将混合液体离心、过滤、去离子水洗涤后置于真空烘箱中干燥。最后采用欠电位沉积方法在所制得的金纳米粒子表面沉积单层铜,在二氧化钛表面不发生沉积,再将其置于含有铂盐的溶液中发生置换反应,使铜被铂置换形成单层铂,重复这一步骤还可在金纳米粒子表面沉积双层铂,制得二氧化钛修饰的金(核)-铂(壳)型催化剂。图2为二氧化钛修饰AuPt核-壳结构金属纳米粒子催化剂的结构示意图。图3为本方法制得二氧化钛修饰的金(核)-铂(壳)型催化剂与商品化Pt催化剂(TanakaKikinzokuInternationalInc.,10E50E,46.6wt%Pt)的氧还原反应性能比较。通过图3可以看出二氧化钛修饰的金(核)-铂(壳)型催化剂的氧还原反应的表面积活性是商品化Pt催化剂的近5倍,氧还原反应的质量活性是商品化Pt催化剂的近10倍。图4为本方法制得二氧化钛修饰的金(核)-铂(壳)型催化剂的稳定性示意图。通过图4可以看出,经过10000圈的电位循环,二氧化钛修饰的金(核)-铂(壳)型催化剂的氧还原反应性能完全没有下降,说明二氧化钛修饰的金(核)-铂(壳)型催化剂具有很好的稳定性。Weigh 140g of carbon black and place it in 50ml of absolute ethanol, after ultrasonication for 60min, add 300mg of sodium citrate to the mixed liquid, and ultrasonication for 30min. Then, 0.3 mmol of titanium isopropoxide was added to the mixed liquid and ultrasonicated for 30 min. Continue to add 2ml of 1mol/L lithium triethyl borohydride to the mixed liquid, add 0.1mmol of sodium chloroaurate after reacting for 30min, and ultrasonicate for 60min. The mixed liquid was centrifuged, filtered, washed with deionized water, and then dried in a vacuum oven. Finally, the underpotential deposition method is used to deposit a single layer of copper on the surface of the prepared gold nanoparticles, and no deposition occurs on the surface of titanium dioxide, and then it is placed in a solution containing a platinum salt to undergo a displacement reaction, so that the copper is replaced by platinum to form a single layer. Platinum, repeating this step can also deposit double-layer platinum on the surface of gold nanoparticles to prepare a titanium dioxide-modified gold (core)-platinum (shell) catalyst. Fig. 2 is a schematic diagram of the structure of a titanium dioxide-modified AuPt core-shell metal nanoparticle catalyst. Figure 3 is a comparison of the oxygen reduction reaction performance of the titania-modified gold (core)-platinum (shell) catalyst prepared by this method and the commercial Pt catalyst (Tanaka Kikinzoku International Inc., 10E50E, 46.6wt%Pt). It can be seen from Figure 3 that the surface area activity of the oxygen reduction reaction of the gold (core)-platinum (shell) catalyst modified by titanium dioxide is nearly 5 times that of the commercial Pt catalyst, and the mass activity of the oxygen reduction reaction is nearly that of the commercial Pt catalyst. 10 times. Figure 4 is a schematic diagram of the stability of the titanium dioxide-modified gold (core)-platinum (shell) catalyst prepared by this method. It can be seen from Figure 4 that after 10,000 potential cycles, the oxygen reduction reaction performance of the titanium dioxide-modified gold (core)-platinum (shell) catalyst has not declined at all, indicating that the titanium dioxide-modified gold (core)-platinum (shell) The catalyst has good stability.
实施例3:Example 3:
称取碳黑140g置于50ml无水乙醇中,超声60min后在混合液体中加入柠檬酸钠300mg,超声30min。然后在混合液体中加入0.8mmol的二氯化钒,超声30min。继续在混合液体中加入3ml1mol/L的三乙基氢化硼锂,超声反应60min后加入0.14mmol的氯金酸钠,超声60min。将混合液体离心、过滤、去离子水洗涤后置于真空烘箱中干燥。最后采用欠电位沉积方法在所制得的金纳米粒子表面沉积单层铜,在氧化钒表面不发生沉积,再将其置于含有铂盐的溶液中发生置换反应,使铜被铂置换形成单层铂,重复这一步骤还可在金纳米粒子表面沉积双层铂,制得氧化钒修饰的金(核)-铂(壳)型催化剂。图5为本方法制得氧化钒修饰的金(核)-铂(壳)型催化剂与商品化Pt催化剂(TanakaKikinzokuInternationalInc.,10E50E,46.6wt%Pt)的氧还原反应性能比较。通过图5可以看出氧化钒修饰的金(核)-铂(壳)型催化剂的氧还原反应的表面积活性是商品化Pt催化剂的5倍多,氧还原反应的质量活性是商品化Pt催化剂的近8倍。图6为本方法制得氧化钒修饰的金(核)-铂(壳)型催化剂的稳定性示意图。通过图6可以看出,经过6000圈的电位循环,氧化钒修饰的金(核)-铂(壳)型催化剂的氧还原反应性能完全没有下降,说明氧化钒修饰的金(核)-铂(壳)型催化剂具有很好的稳定性。Weigh 140g of carbon black and place it in 50ml of absolute ethanol, after ultrasonication for 60min, add 300mg of sodium citrate to the mixed liquid, and ultrasonication for 30min. Then add 0.8 mmol of vanadium dichloride to the mixed liquid, and ultrasonicate for 30 min. Continue to add 3ml of 1mol/L lithium triethyl borohydride to the mixed liquid, and then add 0.14mmol of sodium chloroaurate after ultrasonic reaction for 60 minutes, and ultrasonic for 60 minutes. The mixed liquid was centrifuged, filtered, washed with deionized water, and then dried in a vacuum oven. Finally, the underpotential deposition method is used to deposit a single layer of copper on the surface of the prepared gold nanoparticles, and no deposition occurs on the surface of vanadium oxide, and then it is placed in a solution containing a platinum salt to undergo a displacement reaction, so that the copper is replaced by platinum to form a single layer. Repeating this step can also deposit double-layer platinum on the surface of gold nanoparticles to prepare a vanadium oxide-modified gold (core)-platinum (shell) catalyst. Figure 5 is a comparison of the oxygen reduction reaction performance of the vanadium oxide-modified gold (core)-platinum (shell) catalyst prepared by this method and the commercial Pt catalyst (Tanaka Kikinzoku International Inc., 10E50E, 46.6wt%Pt). It can be seen from Figure 5 that the surface area activity of the oxygen reduction reaction of the vanadium oxide-modified gold (core)-platinum (shell) catalyst is more than five times that of the commercial Pt catalyst, and the mass activity of the oxygen reduction reaction is that of the commercial Pt catalyst. nearly 8 times. Figure 6 is a schematic diagram of the stability of the vanadium oxide-modified gold (core)-platinum (shell) catalyst prepared by this method. It can be seen from Figure 6 that after 6000 cycles of potential cycles, the oxygen reduction reaction performance of the vanadium oxide-modified gold (core)-platinum (shell) catalyst has not declined at all, indicating that the vanadium oxide-modified gold (core)-platinum ( Shell) catalysts have good stability.
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