CN108448126A - A kind of PtAuTi nanowire catalytic material and its preparation method and application as fuel cell catalyst - Google Patents
A kind of PtAuTi nanowire catalytic material and its preparation method and application as fuel cell catalyst Download PDFInfo
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- 239000002070 nanowire Substances 0.000 title claims abstract description 56
- 230000003197 catalytic effect Effects 0.000 title claims abstract description 34
- 239000000463 material Substances 0.000 title claims abstract description 33
- 239000003054 catalyst Substances 0.000 title claims abstract description 29
- 239000000446 fuel Substances 0.000 title claims abstract description 24
- 238000002360 preparation method Methods 0.000 title claims abstract description 17
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 claims abstract description 70
- 239000002243 precursor Substances 0.000 claims abstract description 42
- 229910052697 platinum Inorganic materials 0.000 claims abstract description 30
- 239000002131 composite material Substances 0.000 claims abstract description 25
- 239000002121 nanofiber Substances 0.000 claims abstract description 25
- 239000010936 titanium Substances 0.000 claims abstract description 20
- 239000007788 liquid Substances 0.000 claims abstract description 19
- 229910052751 metal Inorganic materials 0.000 claims abstract description 17
- 239000002184 metal Substances 0.000 claims abstract description 17
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims abstract description 16
- 239000010931 gold Substances 0.000 claims abstract description 16
- 238000010438 heat treatment Methods 0.000 claims abstract description 16
- 229910052719 titanium Inorganic materials 0.000 claims abstract description 16
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 claims abstract description 12
- 229910052737 gold Inorganic materials 0.000 claims abstract description 12
- 239000011230 binding agent Substances 0.000 claims abstract description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 3
- 238000010041 electrostatic spinning Methods 0.000 claims abstract 11
- 238000005253 cladding Methods 0.000 claims abstract 2
- 239000011248 coating agent Substances 0.000 claims abstract 2
- 238000000576 coating method Methods 0.000 claims abstract 2
- 239000002253 acid Substances 0.000 claims description 12
- 238000000034 method Methods 0.000 claims description 8
- NRTOMJZYCJJWKI-UHFFFAOYSA-N Titanium nitride Chemical group [Ti]#N NRTOMJZYCJJWKI-UHFFFAOYSA-N 0.000 claims description 6
- 230000005684 electric field Effects 0.000 claims description 3
- 239000001257 hydrogen Substances 0.000 claims description 3
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- 210000001124 body fluid Anatomy 0.000 claims description 2
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- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims 1
- 240000007594 Oryza sativa Species 0.000 claims 1
- 235000007164 Oryza sativa Nutrition 0.000 claims 1
- FDWREHZXQUYJFJ-UHFFFAOYSA-M gold monochloride Chemical compound [Cl-].[Au+] FDWREHZXQUYJFJ-UHFFFAOYSA-M 0.000 claims 1
- 150000002431 hydrogen Chemical class 0.000 claims 1
- 235000012149 noodles Nutrition 0.000 claims 1
- 150000003057 platinum Chemical class 0.000 claims 1
- 239000011148 porous material Substances 0.000 claims 1
- 235000009566 rice Nutrition 0.000 claims 1
- SDKPSXWGRWWLKR-UHFFFAOYSA-M sodium;9,10-dioxoanthracene-1-sulfonate Chemical compound [Na+].O=C1C2=CC=CC=C2C(=O)C2=C1C=CC=C2S(=O)(=O)[O-] SDKPSXWGRWWLKR-UHFFFAOYSA-M 0.000 claims 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 5
- 239000001301 oxygen Substances 0.000 abstract description 5
- 229910052760 oxygen Inorganic materials 0.000 abstract description 5
- 230000002378 acidificating effect Effects 0.000 abstract description 4
- 230000010757 Reduction Activity Effects 0.000 abstract 1
- 238000006555 catalytic reaction Methods 0.000 abstract 1
- 238000001523 electrospinning Methods 0.000 description 42
- 239000000243 solution Substances 0.000 description 28
- 239000010935 stainless steel Substances 0.000 description 16
- 229910001220 stainless steel Inorganic materials 0.000 description 16
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 7
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- 239000010453 quartz Substances 0.000 description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 4
- 238000005245 sintering Methods 0.000 description 4
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- 229910052782 aluminium Inorganic materials 0.000 description 3
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 3
- ZOMNIUBKTOKEHS-UHFFFAOYSA-L dimercury dichloride Chemical class Cl[Hg][Hg]Cl ZOMNIUBKTOKEHS-UHFFFAOYSA-L 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000000835 electrochemical detection Methods 0.000 description 3
- 239000003792 electrolyte Substances 0.000 description 3
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- 229910021397 glassy carbon Inorganic materials 0.000 description 3
- 239000011259 mixed solution Substances 0.000 description 3
- 238000001878 scanning electron micrograph Methods 0.000 description 3
- 238000005507 spraying Methods 0.000 description 3
- 238000002525 ultrasonication Methods 0.000 description 3
- 229910002844 PtNi Inorganic materials 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000010410 layer Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
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- 239000011865 Pt-based catalyst Substances 0.000 description 1
- 229910018949 PtAu Inorganic materials 0.000 description 1
- 229910002837 PtCo Inorganic materials 0.000 description 1
- 229910002836 PtFe Inorganic materials 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 239000011258 core-shell material Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000002057 nanoflower Substances 0.000 description 1
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- 229920001343 polytetrafluoroethylene Polymers 0.000 description 1
- 239000010970 precious metal Substances 0.000 description 1
- 239000011241 protective layer Substances 0.000 description 1
- 238000011946 reduction process Methods 0.000 description 1
- 150000003839 salts Chemical class 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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- B82Y30/00—Nanotechnology for materials or surface science, e.g. nanocomposites
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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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- 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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Abstract
Description
技术领域technical field
本发明涉及一种燃料电池催化剂材料,特别涉及一种PtAuTi纳米线材料及利用静电纺丝制备PtAuTi纳米线材料的方法,还涉及PtAuTi纳米线材料作为燃料电池催化剂的应用;属于燃料电池催化剂领域。The invention relates to a fuel cell catalyst material, in particular to a PtAuTi nanowire material and a method for preparing the PtAuTi nanowire material by electrospinning, and also relates to the application of the PtAuTi nanowire material as a fuel cell catalyst; it belongs to the field of fuel cell catalysts.
背景技术Background technique
近年来,质子交换膜燃料电池作为理想的绿色能源备受研究人员关注,可应用于交通工具和可移动电子设备。目前,人们常用铂及其合金做质子交换膜燃料电池的电极催化剂,但由于在质子交换燃料电池中存在两个重要问题尚未解决:一方面,由于催化剂的毒化而使得其催化氧还原(ORR)的能力降低;另一方面,催化剂使用贵金属,费用昂贵,从而限制了其工业化发展。因此,当务之急是提高铂催化剂催化氧还原的性能,并减少其使用量。In recent years, proton exchange membrane fuel cells have attracted the attention of researchers as an ideal green energy source, which can be applied to vehicles and mobile electronic devices. At present, platinum and its alloys are often used as electrode catalysts for proton exchange membrane fuel cells, but there are two important problems in proton exchange fuel cells that have not been resolved: on the one hand, due to the poisoning of the catalyst, its catalytic oxygen reduction (ORR) On the other hand, the catalyst uses precious metals, which is expensive, which limits its industrial development. Therefore, it is imperative to improve the performance of platinum catalysts for oxygen reduction and reduce their usage.
目前燃料电池通常使用铂及其合金为催化剂,目前商用化的燃料电池催化剂为20%的铂纳米颗粒直接负载在Carbon XC-72上,但铂资源的匮乏及成本昂贵直接制约了燃料电池技术的推广,阻碍了它的商业化进程。为了降低燃料电池的生产成本,并且保证其具有较好的催化活性,因此,可以提供改进的具有ORR活性的高度稳定的Pt基催化剂具有最可行的研究价值,因为它将降低Pt含量以实现燃料电池性能。近年来,报道很多铂基合金催化剂,如:PtPd、PtAu、PtCo、PtFe、PtNi等,Sa.Liu报道了Pd@PtNi核壳纳米花结构,这种合金结构极大地降低了经济成本,在碱性环境中具有较好的活性,但在酸性环境易被腐蚀。At present, fuel cells usually use platinum and its alloys as catalysts. The current commercial fuel cell catalyst is 20% platinum nanoparticles directly loaded on Carbon XC-72, but the lack of platinum resources and high cost directly restrict the development of fuel cell technology. Promotion hinders its commercialization process. In order to reduce the production cost of fuel cells and ensure its better catalytic activity, therefore, highly stable Pt-based catalysts that can provide improved ORR activity are of the most feasible research value because it will reduce the Pt content to achieve fuel cell battery performance. In recent years, many platinum-based alloy catalysts have been reported, such as: PtPd, PtAu, PtCo, PtFe, PtNi, etc. Sa. Liu reported the Pd@PtNi core-shell nanoflower structure, which greatly reduces the economic cost. It has good activity in acidic environment, but it is easy to be corroded in acidic environment.
发明内容Contents of the invention
针对现有的燃料电池催化剂存在铂含量高、稳定性差等缺陷,本发明的第一个目的是在于提供一种具有一维纳米线状结构,铂含量低,且稳定性好的PtAuTi纳米线催化材料。In view of the defects of high platinum content and poor stability in existing fuel cell catalysts, the first purpose of the present invention is to provide a PtAuTi nanowire catalyst with a one-dimensional nanowire structure, low platinum content and good stability. Material.
本发明的另一目的是在于提供一种简单、低成本的制备所述PtAuTi纳米线催化材料的方法。Another object of the present invention is to provide a simple and low-cost method for preparing the PtAuTi nanowire catalytic material.
本发明的第三个目的是在于提供一种PtAuTi纳米催化材料在燃料电池中的应用,其具有铂含量低、催化性能好、稳定性高等特点。The third object of the present invention is to provide a PtAuTi nano catalytic material for application in fuel cells, which has the characteristics of low platinum content, good catalytic performance and high stability.
为了实现上述技术目的,本发明提供了一种PtAuTi纳米线催化材料,其由碳层包覆金属纳米线构成;所述金属纳米线由铂、金和钛三种金属混合构成。In order to achieve the above technical purpose, the present invention provides a PtAuTi nanowire catalytic material, which is composed of metal nanowires coated with a carbon layer; the metal nanowires are composed of platinum, gold and titanium.
本发明的PtAuTi纳米线催化材料具有一维金属纳米线状结构,且表面包有一层薄薄的碳层作为保护层,能提高催化材料的稳定性。The PtAuTi nanowire catalytic material of the invention has a one-dimensional metal nanowire structure, and the surface is covered with a thin carbon layer as a protective layer, which can improve the stability of the catalytic material.
优选的方案,铂、金和钛的摩尔比为1:0.1~10:0.1~10;优选为1:1~2:1~2;最优选为1:1.5:1.5。本发明的PtAuTi纳米线催化材料在铂、金和钛摩尔比为1:1.5:1.5时具有最佳的氧还原催化性能,且相对现有的铂金属类催化剂铂含量大大降低。In a preferred solution, the molar ratio of platinum, gold and titanium is 1:0.1-10:0.1-10; preferably 1:1-2:1-2; most preferably 1:1.5:1.5. The PtAuTi nanowire catalytic material of the present invention has the best oxygen reduction catalytic performance when the molar ratio of platinum, gold and titanium is 1:1.5:1.5, and the platinum content is greatly reduced compared with the existing platinum metal catalysts.
本发明还提供了一种PtAuTi纳米线催化材料的制备方法,其包括以下步骤:The present invention also provides a preparation method of PtAuTi nanowire catalytic material, which comprises the following steps:
1)将铂源、金源和钛源及粘结剂溶于水中,得到静电纺丝前驱液;1) dissolving platinum source, gold source, titanium source and binder in water to obtain electrospinning precursor;
2)所述静电纺丝前驱体液通过静电纺丝,得到复合纳米纤维;2) The electrospinning precursor fluid is electrospun to obtain composite nanofibers;
3)所述复合纳米纤维通过热处理,得到纳米线;3) The composite nanofibers are heat-treated to obtain nanowires;
4)将纳米线通过还原处理,即得。4) The nanowires are obtained through reduction treatment.
优选的方案,所述静电纺丝前驱液中铂源、金源和钛源的总质量分数为3wt%~6wt%,粘结剂的质量分数为4wt%~10wt%。铂源、金源和钛源的总质量分数优选为3wt%。粘结剂的质量分数优选为6wt%。一般的铂源、金源和钛源为水溶性的含铂、金或钛的化合物,如金属盐或酸类化合物。优选的铂源为氯铂酸。优选的金源为氯金酸。优选的钛源为氮化钛。In a preferred solution, the total mass fraction of platinum source, gold source and titanium source in the electrospinning precursor solution is 3wt%-6wt%, and the mass fraction of the binder is 4wt%-10wt%. The total mass fraction of platinum source, gold source and titanium source is preferably 3wt%. The mass fraction of the binder is preferably 6 wt%. Common sources of platinum, gold and titanium are water-soluble compounds containing platinum, gold or titanium, such as metal salts or acid compounds. A preferred source of platinum is chloroplatinic acid. A preferred gold source is chloroauric acid. A preferred source of titanium is titanium nitride.
所述的粘结剂为可以通过静电纺丝的高分子材料,包括PVP、PVA、PAN、PVB、PMMA中至少一种。The binder is a polymer material that can be electrospun, including at least one of PVP, PVA, PAN, PVB, and PMMA.
优选的方案,所述静电纺丝包括A或B方案:Preferred scheme, described electrospinning comprises A or B scheme:
A方案:将静电纺丝前驱体液装入喷液装置中,喷液装置设置在静电纺丝机上,与负极相连,在喷液装置的喷头与正极的接受装置之间施加恒定的直流电压,从接受装置上得到复合纳米纤维;Solution A: Put the body fluid of the electrospinning precursor into the liquid spraying device. The liquid spraying device is set on the electrospinning machine and connected to the negative electrode. A constant DC voltage is applied between the nozzle of the liquid spraying device and the receiving device of the positive electrode. Composite nanofibers are obtained on the receiving device;
B方案:将静电纺丝前驱体液置入溶液槽内,将与正极相连的滚筒浸入到静电纺丝前驱体液中,滚筒转动,在离心力的和电场的作用下抽拉固化成丝,得到复合纳米纤维。Plan B: Put the electrospinning precursor liquid into the solution tank, immerse the roller connected to the positive electrode into the electrospinning precursor liquid, rotate the roller, pull and solidify into filaments under the action of centrifugal force and electric field, and obtain composite nano fiber.
较优选的方案,A方案中,喷头口孔径大小为0.2mm~1.86mm,恒定电压为6KV~100KV,喷头与正极之间的距离为10cm~100cm,静电纺丝前驱液的推进速度为0.3~3mL/h。The more preferred scheme, in scheme A, the aperture size of the nozzle opening is 0.2mm-1.86mm, the constant voltage is 6KV-100KV, the distance between the nozzle and the positive electrode is 10cm-100cm, and the propulsion speed of the electrospinning precursor is 0.3-100cm. 3mL/h.
较优选的方案,B方案中,滚筒直径为10~80cm,正负极之间的电压为6KV~100KV,正负极之间的距离为30~180cm。A more preferred scheme, in scheme B, the diameter of the drum is 10-80cm, the voltage between the positive and negative electrodes is 6KV-100KV, and the distance between the positive and negative electrodes is 30-180cm.
优选的方案,所述热处理过程为:复合纳米纤维在空气气氛下,以0.2℃/min~2℃/min的升温速度升温至200℃~300℃,保温0.5~1.5h,再以0.5℃/min~3℃/min的升温速度升温至500℃~700℃恒温烧结2h~4h。In a preferred scheme, the heat treatment process is as follows: the composite nanofiber is heated to 200°C to 300°C at a heating rate of 0.2°C/min to 2°C/min in an air atmosphere, kept for 0.5 to 1.5h, and then heated at a temperature of 0.5°C/min to 200°C to 300°C. Min ~ 3 ℃ / min temperature rise rate to 500 ℃ ~ 700 ℃ constant temperature sintering 2h ~ 4h.
优选的方案,所述还原过程为:将纳米线置于含氢气的气氛下,在150℃~300℃温度下保温2h~3h。In a preferred solution, the reduction process is as follows: placing the nanowires in an atmosphere containing hydrogen, and keeping the temperature at 150° C. to 300° C. for 2 hours to 3 hours.
本发明还提供了一种PtAuTi纳米线催化材料的应用,将其作为燃料电池催化剂应用。The invention also provides an application of the PtAuTi nanowire catalytic material, which is used as a fuel cell catalyst.
本发明的PtAuTi纳米线催化材料的制备方法,包括以下工艺步骤:The preparation method of the PtAuTi nanowire catalytic material of the present invention comprises the following process steps:
一、静电纺丝前驱液的制备:1. Preparation of electrospinning precursor solution:
按照Pt:Au:Ti=1:0.1~10:0.1~10的摩尔比,分别称取前驱体氯铂酸、氯金酸、氮化钛溶解在水溶液中,将一定量的粘结剂缓慢加入前驱液中,搅拌12h使其充分溶解后得到透明的静电纺丝前驱液;静电纺丝前驱液中金属前驱体的质量分数为3wt%~6wt%,粘结剂的质量分数为4wt%~10wt%;粘结剂为PVP、PVA、PAN、PVB、PMMA等一系列可用于静电纺丝的高分子;According to the molar ratio of Pt:Au:Ti=1:0.1~10:0.1~10, the precursors of chloroplatinic acid, chloroauric acid and titanium nitride were respectively weighed and dissolved in the aqueous solution, and a certain amount of binder was added slowly In the precursor solution, stir for 12 hours to fully dissolve to obtain a transparent electrospinning precursor solution; the mass fraction of the metal precursor in the electrospinning precursor solution is 3wt% to 6wt%, and the mass fraction of the binder is 4wt% to 10wt% %; the binder is a series of polymers that can be used for electrospinning such as PVP, PVA, PAN, PVB, PMMA;
二、静电纺丝2. Electrospinning
将步骤一中得到的静电纺丝前驱体液注入到带有不锈钢针头的注射器中,将注射器安置在静电纺丝机上,与负极相连,在不锈钢针头与正极的接受装置之间施加恒定的直流电压,通过旋转接受装置,得到复合纳米纤维;不锈钢针头大小为0.20mm~1.86mm,恒定电压为6KV~100KV,不锈钢针头与正极之间的距离为10cm~100cm,静电纺丝溶液的推进速度为0.3~3mL/h;接收装置为炭纸、铝箔、高导电的PI膜包覆的金属滚筒或直接铁丝网、炭纸铝箔覆盖的平面接收装置;Inject the electrospinning precursor liquid obtained in step 1 into a syringe with a stainless steel needle, place the syringe on the electrospinning machine, connect it to the negative electrode, and apply a constant DC voltage between the stainless steel needle and the receiving device of the positive electrode, Composite nanofibers are obtained by rotating the receiving device; the size of the stainless steel needle is 0.20mm-1.86mm, the constant voltage is 6KV-100KV, the distance between the stainless steel needle and the positive electrode is 10cm-100cm, and the advancing speed of the electrospinning solution is 0.3- 3mL/h; the receiving device is a metal roller covered by carbon paper, aluminum foil, highly conductive PI film or a flat receiving device covered by direct barbed wire or carbon paper and aluminum foil;
或者,将静电纺丝前驱体液置入溶液槽内,将与正极相连的滚筒浸入到静电纺丝前驱体液中,滚筒转动,在离心力的和电场的作用下抽拉固化成丝,得到复合纳米纤维;滚筒直径为10~80cm,正负极之间的电压为6KV~100KV,正负极之间的距离为30~180cm;Alternatively, put the electrospinning precursor liquid into the solution tank, immerse the drum connected to the positive electrode into the electrospinning precursor liquid, rotate the drum, pull and solidify into filaments under the action of centrifugal force and electric field, and obtain composite nanofibers ; The diameter of the drum is 10-80cm, the voltage between the positive and negative electrodes is 6KV-100KV, and the distance between the positive and negative electrodes is 30-180cm;
三、热处理3. Heat treatment
将步骤二中的复合纳米纤维收集于石英舟中,将其置于管式炉中,以0.2℃/min~2℃/min的速度在空气中升温至200℃~300℃,然后保温1h,然后再以0.5℃/min~3℃/min的升温速度在空气中升温至500℃~700℃恒温烧结2h~4h,即可除去复合纳米纤维中的PVP。Collect the composite nanofibers in step 2 in a quartz boat, place it in a tube furnace, raise the temperature to 200°C to 300°C in air at a rate of 0.2°C/min to 2°C/min, and then keep it warm for 1h. Then heat up to 500°C-700°C in air at a heating rate of 0.5°C/min-3°C/min and sinter at a constant temperature for 2h-4h to remove the PVP in the composite nanofibers.
四、H2还原4. H2 Reduction
将步骤三中得到的纳米线冷却至150℃~300℃,通入稀释过的H2保温2h~3h,将其还原得到PtAuTi-NWs;稀释过H2为H2与N2或Ar的混合气体,气体的流量为0.1~2L/min。Cool the nanowires obtained in step 3 to 150°C to 300°C, pass through diluted H 2 for 2h to 3h, and then reduce them to obtain PtAuTi-NWs; dilute H 2 to form a mixture of H 2 and N 2 or Ar Gas, the gas flow rate is 0.1~2L/min.
相对现有技术,本发明的技术方案带来的有益技术效果:Compared with the prior art, the beneficial technical effect brought by the technical solution of the present invention:
1)本发明的PtAuTi纳米线催化材料具有稳定性好,特别是酸性体系中可以稳定存在,催化活性高的特点,可以作为燃料电池氧还原催化剂广泛应用。1) The PtAuTi nanowire catalytic material of the present invention has the characteristics of good stability, especially stable existence in an acidic system, and high catalytic activity, and can be widely used as an oxygen reduction catalyst for fuel cells.
2)本发明的PtAuTi纳米线催化材料相对现有技术中的铂金属催化剂铂含量低,催化活性高,大大降低了催化材料的使用成本。2) Compared with the platinum metal catalyst in the prior art, the PtAuTi nanowire catalytic material of the present invention has lower platinum content and higher catalytic activity, which greatly reduces the use cost of the catalytic material.
3)本发明的PtAuTi纳米线催化材料可以采用静电纺丝技术制得,具有制备方便,操作简单,可批量生产的优点。3) The PtAuTi nanowire catalytic material of the present invention can be prepared by electrospinning technology, and has the advantages of convenient preparation, simple operation and mass production.
附图说明Description of drawings
【图1】为实施例1制备的PtAuTi纳米线燃料电池催化剂的扫描电镜图。[Fig. 1] is a scanning electron micrograph of the PtAuTi nanowire fuel cell catalyst prepared in Example 1.
【图2】为实施例2制备的PtAuTi纳米线燃料电池催化剂的扫描电镜图。[Fig. 2] is the scanning electron micrograph of the PtAuTi nanowire fuel cell catalyst prepared in Example 2.
【图3】为实施例3制备的PtAuTi纳米线燃料电池催化剂的扫描电镜图。[ Fig. 3 ] is a scanning electron micrograph of the PtAuTi nanowire fuel cell catalyst prepared in Example 3.
【图4】为实施例1制备的PtAuTi纳米线燃料电池催化剂与20%Pt/C的CV对比图。[ Fig. 4 ] is the CV comparison chart of the PtAuTi nanowire fuel cell catalyst prepared in Example 1 and 20% Pt/C.
【图5】为实施例2制备的PtAuTi纳米线燃料电池催化剂与20%Pt/C的CV对比图。[ Fig. 5 ] is the CV comparison chart of the PtAuTi nanowire fuel cell catalyst prepared in Example 2 and 20% Pt/C.
【图6】为实施例3制备的PtAuTi纳米线燃料电池催化剂与20%Pt/C的CV对比图。[ Fig. 6 ] is the CV comparison chart of the PtAuTi nanowire fuel cell catalyst prepared in Example 3 and 20% Pt/C.
具体实施方式Detailed ways
下面结合非限制性的具体实施例进一步示例性地详细说明本发明。The present invention will be further illustrated in detail below in conjunction with non-limiting specific examples.
本发明实施例中所使用的试剂均可市购得到。The reagents used in the examples of the present invention are all commercially available.
实施例1Example 1
一、静电纺丝前驱液的制备1. Preparation of electrospinning precursor solution
按照Pt:Au:Ti=1:1:0.5的摩尔比,分别称取159mg氯铂酸、122mg氯金酸、9mg氮化钛溶解在10mL水溶液中,将0.6g的PVP缓慢加入前驱液中,搅拌12h使其充分溶解后得到透明的静电纺丝前驱液;所述的静电纺丝前驱液中金属前驱体的质量百分比浓度为3%,PVP的质量百分比浓度为6%。According to the molar ratio of Pt:Au:Ti=1:1:0.5, respectively weigh 159mg of chloroplatinic acid, 122mg of chloroauric acid, and 9mg of titanium nitride and dissolve them in 10mL of aqueous solution, and slowly add 0.6g of PVP into the precursor solution, After stirring for 12 hours to fully dissolve, a transparent electrospinning precursor solution was obtained; the mass percent concentration of the metal precursor in the electrospinning precursor solution was 3%, and the mass percent concentration of PVP was 6%.
二、静电纺丝2. Electrospinning
将步骤一中得到的静电纺丝前驱体液注入到带有的不锈钢针头的注射器中,将注射器安置在静电纺丝机上,与负极相连,在不锈钢针头与正极的接受装置之间施加恒定的直流电压,通过旋转接受装置(炭纸),得到复合纳米纤维。所述的不锈钢针头的大小为0.5mm,直流电压为25KV,不锈钢针头与接收装置之间的距离为15cm,静电纺丝溶液的推进速度为1mL/h装置内温度为25℃,相对湿度为30%。Inject the electrospinning precursor liquid obtained in step 1 into a syringe with a stainless steel needle, place the syringe on the electrospinning machine, connect it to the negative electrode, and apply a constant DC voltage between the stainless steel needle and the receiving device of the positive electrode , by rotating the receiving device (carbon paper) to obtain composite nanofibers. The size of the stainless steel needle is 0.5mm, the DC voltage is 25KV, the distance between the stainless steel needle and the receiving device is 15cm, the advancing speed of the electrospinning solution is 1mL/h, the temperature inside the device is 25°C, and the relative humidity is 30°C. %.
三、热处理3. Heat treatment
将步骤二中的复合纳米纤维收集于石英舟中,将其置于管式炉中,以1℃/min的速度在空气中升温至200℃,然后保温1h,然后再以1℃/min的升温速度在空气中升温至500℃恒温烧结2h,即可除去复合纳米纤维中的PVP。Collect the composite nanofibers in step 2 in a quartz boat, place it in a tube furnace, heat up to 200°C in air at a rate of 1°C/min, then keep it warm for 1h, and then heat it up at a rate of 1°C/min. Heating rate Heating up to 500°C in air and sintering at a constant temperature for 2 hours can remove the PVP in the composite nanofibers.
四、H2还原4. H2 Reduction
将步骤三中得到的纳米线冷却至150℃,通入稀释过的H2保温2h,将其还原得到PtAuTi-NWs。Cool the nanowires obtained in step 3 to 150° C., pass through diluted H 2 for 2 hours, and reduce them to obtain PtAuTi-NWs.
五、电化学检测5. Electrochemical detection
取2mg制得的纳米线,分散在1ml的nafion水溶液(1:9)中,超声半个小时后,取15μl的混合溶液滴于玻炭电极上,自然干燥后,用电化学工作站测纳米线催化剂的电化学性能,其中以饱和甘汞电极为参比电极,铂片为对极,0.1M的HCLO4为电解液,扫速为0.01V/S。Take 2 mg of the prepared nanowires and disperse them in 1 ml of nafion aqueous solution (1:9). After ultrasonication for half an hour, take 15 μl of the mixed solution and drop it on a glassy carbon electrode. After natural drying, use an electrochemical workstation to measure the nanowires The electrochemical performance of the catalyst, wherein the saturated calomel electrode is used as the reference electrode, the platinum sheet is used as the counter electrode, 0.1M HCLO 4 is used as the electrolyte, and the scan rate is 0.01V/S.
实施例2Example 2
一、静电纺丝前驱液的制备1. Preparation of electrospinning precursor solution
按照Pt:Au:Ti=1:1:1的摩尔比,分别称取159mg氯铂酸、122mg氯金酸、18mg氮化钛溶解在10mL水溶液中,将0.5g的PVP缓慢加入前驱液中,搅拌12h使其充分溶解后得到透明的静电纺丝前驱液;所述的静电纺丝前驱液中金属前驱体的质量浓度为3%,PVP的质量浓度为5%。According to the molar ratio of Pt:Au:Ti=1:1:1, weigh 159mg of chloroplatinic acid, 122mg of chloroauric acid, and 18mg of titanium nitride and dissolve them in 10mL of aqueous solution, and slowly add 0.5g of PVP into the precursor solution. Stir for 12 hours to fully dissolve to obtain a transparent electrospinning precursor solution; the mass concentration of the metal precursor in the electrospinning precursor solution is 3%, and the mass concentration of PVP is 5%.
二、静电纺丝2. Electrospinning
将步骤一中得到的静电纺丝前驱体液注入到带有的不锈钢针头的注射器中,将注射器安置在静电纺丝机上,与负极相连,在不锈钢针头与正极的接受装置之间施加恒定的直流电压,通过旋转接受装置(炭纸),得到复合纳米纤维。所述的不锈钢针头的大小为0.8mm,直流电压为60KV,不锈钢针头与接收装置之间的距离为30cm,静电纺丝溶液的推进速度为0.5mL/h,装置内温度为25℃,相对湿度为30%。Inject the electrospinning precursor liquid obtained in step 1 into a syringe with a stainless steel needle, place the syringe on the electrospinning machine, connect it to the negative electrode, and apply a constant DC voltage between the stainless steel needle and the receiving device of the positive electrode , by rotating the receiving device (carbon paper) to obtain composite nanofibers. The size of the stainless steel needle is 0.8mm, the DC voltage is 60KV, the distance between the stainless steel needle and the receiving device is 30cm, the advancing speed of the electrospinning solution is 0.5mL/h, the temperature inside the device is 25°C, and the relative humidity 30%.
三、热处理3. Heat treatment
将步骤二中的复合纳米纤维收集于石英舟中,将其置于管式炉中,以1℃/min的速度在空气中升温至250℃,然后保温1h,然后再以1℃/min的升温速度在空气中升温至600℃恒温烧结2h,即可除去复合纳米纤维中的PVP。Collect the composite nanofibers in step 2 in a quartz boat, place it in a tube furnace, raise the temperature to 250°C in air at a rate of 1°C/min, keep it warm for 1h, and then heat it up at a rate of 1°C/min. Heating rate The PVP in the composite nanofibers can be removed by raising the temperature to 600° C. in the air and sintering at a constant temperature for 2 hours.
四、H2还原4. H2 Reduction
将步骤三中得到的纳米线冷却至250℃,通入稀释过的H2保温2h,将其还原得到PtAuTi-NWs。Cool the nanowires obtained in step 3 to 250°C, pass through diluted H 2 for 2 hours, and reduce them to obtain PtAuTi-NWs.
五、电化学检测5. Electrochemical detection
取2mg制得的纳米线,分散在1ml的nafion水溶液(1:9)中,超声半个小时后,取15μl的混合溶液滴于玻炭电极上,自然干燥后,用电化学工作站测纳米线催化剂的电化学性能,其中以饱和甘汞电极为参比电极,铂片为对极,0.1M的HCLO4为电解液,扫速为0.01V/S。Take 2 mg of the prepared nanowires and disperse them in 1 ml of nafion aqueous solution (1:9). After ultrasonication for half an hour, take 15 μl of the mixed solution and drop it on the glassy carbon electrode. After natural drying, use an electrochemical workstation to measure the nanowires The electrochemical performance of the catalyst, wherein the saturated calomel electrode is used as the reference electrode, the platinum sheet is used as the counter electrode, 0.1M HCLO4 is used as the electrolyte, and the scan rate is 0.01V/S.
实施例3Example 3
一、静电纺丝前驱液的制备1. Preparation of electrospinning precursor solution
按照Pt:Au:Ti=1:1:2的摩尔比,分别称取159mg氯铂酸、122mg氯金酸、36mg氮化钛溶解在10mL水溶液中,将0.6g的PVA缓慢加入前驱液中,搅拌12h使其充分溶解后得到透明的静电纺丝前驱液;所述的静电纺丝前驱液中金属前驱体的质量浓度为3%,PVA的质量浓度为6%。According to the molar ratio of Pt:Au:Ti=1:1:2, weigh 159mg of chloroplatinic acid, 122mg of chloroauric acid, and 36mg of titanium nitride and dissolve them in 10mL of aqueous solution, and slowly add 0.6g of PVA into the precursor solution. Stir for 12 hours to fully dissolve to obtain a transparent electrospinning precursor solution; the mass concentration of the metal precursor in the electrospinning precursor solution is 3%, and the mass concentration of PVA is 6%.
二、静电纺丝2. Electrospinning
将步骤一中得到的静电纺丝前驱体液注入到带有的不锈钢针头的注射器中,将注射器安置在静电纺丝机上,与负极相连,在不锈钢针头与正极的接受装置之间施加恒定的直流电压,通过旋转接受装置(铝箔),得到复合纳米纤维。所述的不锈钢针头的大小为0.5mm,直流电压为20KV,不锈钢针头与接收装置之间的距离为15cm,静电纺丝溶液的推进速度为1.5mL/h装置内温度为25℃,相对湿度为30%。Inject the electrospinning precursor liquid obtained in step 1 into a syringe with a stainless steel needle, place the syringe on the electrospinning machine, connect it to the negative electrode, and apply a constant DC voltage between the stainless steel needle and the receiving device of the positive electrode , by rotating the receiving device (aluminum foil) to obtain composite nanofibers. The size of the stainless steel needle is 0.5mm, the DC voltage is 20KV, the distance between the stainless steel needle and the receiving device is 15cm, the advancing speed of the electrospinning solution is 1.5mL/h, the temperature in the device is 25°C, and the relative humidity is 30%.
三、热处理3. Heat treatment
将步骤二中的复合纳米纤维收集于石英舟中,将其置于管式炉中,以1℃/min的速度在空气中升温至200℃,然后保温1h,然后再以1℃/min的升温速度在空气中升温至500℃恒温烧结2h,即可除去复合纳米纤维中的PVA。Collect the composite nanofibers in step 2 in a quartz boat, place it in a tube furnace, heat up to 200°C in air at a rate of 1°C/min, then keep it warm for 1h, and then heat it up at a rate of 1°C/min. Heating rate Heating up to 500°C in air and sintering at a constant temperature for 2 hours can remove the PVA in the composite nanofibers.
四、H2还原4. H2 Reduction
将步骤三中得到的纳米线冷却至150℃,通入稀释过的H2保温2h,将其还原得到PtAuTi-NWs。Cool the nanowires obtained in step 3 to 150° C., pass through diluted H 2 for 2 hours, and reduce them to obtain PtAuTi-NWs.
五、电化学检测5. Electrochemical detection
取2mg制得的纳米线,分散在1ml的nafion水溶液(1:9)中,超声半个小时后,取15μl的混合溶液滴于玻炭电极上,自然干燥后,用电化学工作站测纳米线催化剂的电化学性能,其中以饱和甘汞电极为参比电极,铂片为对极,0.1M的HCLO4为电解液,扫速为0.01V/S。Take 2 mg of the prepared nanowires and disperse them in 1 ml of nafion aqueous solution (1:9). After ultrasonication for half an hour, take 15 μl of the mixed solution and drop it on the glassy carbon electrode. After natural drying, use an electrochemical workstation to measure the nanowires The electrochemical performance of the catalyst, wherein the saturated calomel electrode is used as the reference electrode, the platinum sheet is used as the counter electrode, 0.1M HCLO4 is used as the electrolyte, and the scan rate is 0.01V/S.
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