CN102626649A - Oxygen reduction non-noble metal catalyst and preparation method thereof - Google Patents
Oxygen reduction non-noble metal catalyst and preparation method thereof Download PDFInfo
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- 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
本发明提供一种氧还原非贵金属催化剂及其制备方法,属于燃料电池技术领域。通过将含氮单体引入层状无机化合物层间,层间聚合热解形成具有类石墨结构的氮掺杂非贵金属燃料电池催化剂。利用层状化合物的近乎封闭效应,有效地降低活性氮损失提高催化剂石墨化程度,从而提高非贵金属催化剂的催化活性和稳定性。本发明方法简单易行,生产成本低廉,采用本发明制备的催化剂具有良好的氧还原催化活性与稳定性,可应用于以质子交换膜为电解质的燃料电池。用本发明制造的燃料电池,广泛应用于电动汽车,各种航天器,便携式电子设备,如摄像机,笔记本电脑,电动玩具等。The invention provides an oxygen reduction non-noble metal catalyst and a preparation method thereof, belonging to the technical field of fuel cells. A nitrogen-doped non-precious metal fuel cell catalyst with a graphite-like structure is formed by introducing a nitrogen-containing monomer into the interlayer of a layered inorganic compound, and interlayer polymerization and pyrolysis. The near-sealing effect of the layered compound is used to effectively reduce the loss of active nitrogen and improve the degree of graphitization of the catalyst, thereby improving the catalytic activity and stability of the non-noble metal catalyst. The method of the invention is simple and easy, and the production cost is low. The catalyst prepared by the invention has good oxygen reduction catalytic activity and stability, and can be applied to fuel cells using proton exchange membranes as electrolytes. The fuel cell manufactured by the invention is widely used in electric automobiles, various spacecraft, portable electronic equipment, such as video cameras, notebook computers, electric toys and the like.
Description
一、技术领域: 1. Technical field:
本发明属于燃料电池技术领域,特别涉及一种氧还原非贵金属催化剂及其制备方法。The invention belongs to the technical field of fuel cells, in particular to an oxygen-reducing non-noble metal catalyst and a preparation method thereof.
二、背景技术: 2. Background technology:
燃料电池具有能量转换效率高、环境友好、室温快速启动等优点,被认为是未来电动汽车及其它民用场合最有希望的化学电源。目前,主要的质子交换膜燃料电池(PEMFCs)阴极催化剂是铂类催化剂,但其高昂的成本、资源匮乏和易中毒等缺点严重制约了燃料电池的发展。因此,开发一种成本低廉且性能优异的PEMFCs阴极非贵金属催化剂具有重要意义。Fuel cells have the advantages of high energy conversion efficiency, environmental friendliness, and rapid start-up at room temperature, and are considered to be the most promising chemical power sources for electric vehicles and other civilian applications in the future. At present, the main cathode catalysts for proton exchange membrane fuel cells (PEMFCs) are platinum-based catalysts, but their disadvantages such as high cost, lack of resources, and easy poisoning seriously restrict the development of fuel cells. Therefore, it is of great significance to develop a low-cost and high-performance non-noble metal catalyst for PEMFCs cathode.
近年来国内外针对非贵金属催化剂做了大量的研究。中国发明专利201110138139.9公开了“一种碳载CoN燃料电池催化剂及其制备方法和应用”,在惰性气体气氛保护下,通过高温热处理Co金属盐类、氮化合物以及碳材料的混合物形成碳负载CoN燃料电池催化剂。该方法制备的碳负载CoN燃料电池催化剂在碱性环境中具有一定的催化氧还原活性。但是,在酸性条件下金属Co的溶出将严重影响催化剂的稳定性与活性。中国发明专利200610113692.6公开了“一种直接甲醇燃料电池阴极非贵金属催化剂及其制备方法”,通过在氨气气氛下热处理过渡金属大环化合物与Vulcan XC-72活性碳粉混合物,形成碳负载型过渡金属氮化物催化剂。该方法制备的碳负载型过渡金属氮化物催化剂具有一定的氧还原活性,但是,催化剂中存在的自由金属离子将极大的加速电解质膜衰减老化,降低燃料电池寿命。因而,采用上述方法所得催化剂的与燃料电池催化剂要求仍然存在一定差距。In recent years, a lot of research has been done on non-precious metal catalysts at home and abroad. Chinese invention patent 201110138139.9 discloses "a carbon-supported CoN fuel cell catalyst and its preparation method and application". Under the protection of an inert gas atmosphere, carbon-supported CoN fuel is formed by high-temperature heat treatment of a mixture of Co metal salts, nitrogen compounds and carbon materials battery catalyst. The carbon-supported CoN fuel cell catalyst prepared by this method has certain catalytic oxygen reduction activity in alkaline environment. However, the dissolution of metal Co under acidic conditions will seriously affect the stability and activity of the catalyst. Chinese invention patent 200610113692.6 discloses "a non-precious metal catalyst for direct methanol fuel cell cathode and its preparation method". The carbon-supported transition Metal Nitride Catalysts. The carbon-loaded transition metal nitride catalyst prepared by the method has a certain oxygen reduction activity, but the free metal ions in the catalyst will greatly accelerate the attenuation and aging of the electrolyte membrane and reduce the service life of the fuel cell. Therefore, there is still a certain gap between the catalyst obtained by the above method and the fuel cell catalyst requirements.
三、发明内容: 3. Contents of the invention:
本发明的目的是针对现有燃料电池Pt/C催化剂成本高昂资源匮乏的缺点,提供一种氧还原非贵金属催化剂及其制备方法。本发明首先将吡咯或苯胺单体引入层状无机化合物的层间,然后通过化学氧化聚合的方法在层间形成具有二维特性的聚吡咯或聚苯胺前驱体,最后在高温下热解形成具有类石墨结构的氮掺杂非贵金属燃料电池催化剂。本发明选择具有类石墨结构、易于石墨化的聚吡咯或聚苯胺为含氮前驱体,巧妙利用层状无机化合物特有的空间限域作用制备尺寸及厚度可控的纳米片层类石墨结构,同时利用层状无机化合物近乎封闭的结构有效降低热解过程中的活性氮损失,提高活性氮的含量,从而提高非贵金属催化剂的催化活性和稳定性。The object of the present invention is to provide an oxygen-reducing non-noble metal catalyst and a preparation method thereof, aiming at the disadvantages of the existing fuel cell Pt/C catalysts, which are high in cost and lack of resources. In the present invention, firstly, pyrrole or aniline monomer is introduced into the interlayer of the layered inorganic compound, and then a polypyrrole or polyaniline precursor with two-dimensional characteristics is formed between the layers through chemical oxidation polymerization, and finally pyrolyzed at high temperature to form a polypyrrole or polyaniline precursor with Nitrogen-doped non-noble metal fuel cell catalysts with graphite-like structure. The present invention selects polypyrrole or polyaniline, which has a graphite-like structure and is easy to graphitize, as a nitrogen-containing precursor, and cleverly utilizes the unique space confinement effect of layered inorganic compounds to prepare a nano-sheet graphite-like structure with controllable size and thickness. The nearly closed structure of the layered inorganic compound is used to effectively reduce the loss of active nitrogen during the pyrolysis process and increase the content of active nitrogen, thereby improving the catalytic activity and stability of the non-noble metal catalyst.
本发明的目的是这样实现的:一种氧还原非贵金属催化剂及其制备方法,其具体方法步骤包括:The object of the present invention is achieved in that a kind of oxygen-reducing non-precious metal catalyst and preparation method thereof, its specific method step comprises:
(1)苯胺或吡咯插层的层状化合物悬浮液制备(1) Preparation of layered compound suspensions intercalated with aniline or pyrrole
按层状化合物∶苯胺或吡咯的质量比为1∶0.1~4称取层状化合物和苯胺或吡咯,先将层状化合物分散在去离子水中,超声搅拌3~8小时形成质量浓度为0.01~0.1克/毫升的层状化合物悬浮液;按层状化合物悬浮液∶乙醇或丙酮或乙腈的体积比为1∶0.3~1量取乙醇或丙酮或乙腈,将苯胺或吡咯溶于乙醇或丙酮或乙腈中,并加入到上述层状化合物悬浮液中,10~60℃搅拌10~40小时,形成苯胺或吡咯插层的层状化合物悬浮液。Weigh the layered compound and aniline or pyrrole according to the mass ratio of layered compound: aniline or pyrrole is 1:0.1~4, first disperse the layered compound in deionized water, and stir ultrasonically for 3~8 hours to form a mass concentration of 0.01~ 0.1 g/ml layered compound suspension; measure ethanol or acetone or acetonitrile according to the volume ratio of layered compound suspension: ethanol or acetone or acetonitrile, and dissolve aniline or pyrrole in ethanol or acetone or acetonitrile, and added to the layered compound suspension, stirred at 10-60°C for 10-40 hours to form a layered compound suspension intercalated with aniline or pyrrole.
(2)苯胺或吡咯层间聚合(2) Interlayer polymerization of aniline or pyrrole
按步骤(1)所获得的苯胺或吡咯插层的层状化合物悬浮液∶硫酸或盐酸溶液的体积比1∶0.1~0.5量取硫酸或盐酸溶液,其中硫酸或盐酸溶液浓度为0.5~1.5摩尔/升;按苯胺或吡咯∶氧化剂的质量比为1∶0.5~2称取氧化剂,并溶于去离子水中形成质量浓度为0.1~1克/毫升氧化剂溶液;先将硫酸或盐酸溶液加入到步骤(1)所获得的苯胺或吡咯插层的层状化合物悬浮液中,搅拌1~3小时,再将氧化剂溶液以0.1~1毫升/分钟速度加入上述悬浮液中,0~10℃搅拌反应10~30小时,最后经真空抽滤,去离子水洗涤3次和无水乙醇洗涤3次,60℃干燥24小时,研磨后获得层状化合物夹层聚苯胺或聚吡咯。The layered compound suspension of the aniline or pyrrole intercalation obtained in step (1): the volume ratio of sulfuric acid or hydrochloric acid solution is 1: 0.1~0.5 Measure sulfuric acid or hydrochloric acid solution, wherein the concentration of sulfuric acid or hydrochloric acid solution is 0.5~1.5 moles per liter; by aniline or pyrrole: the mass ratio of oxidant is 1: 0.5~2 to take oxidant, and be dissolved in deionized water to form mass concentration and be 0.1~1 g/ml oxidant solution; Sulfuric acid or hydrochloric acid solution is added to step (1) In the layered compound suspension obtained by aniline or pyrrole intercalation, stir for 1 to 3 hours, then add the oxidizing agent solution to the suspension at a rate of 0.1 to 1 ml/min, and stir at 0 to 10°C for 10 ~ 30 hours, and finally vacuum filtered, washed three times with deionized water and three times with absolute ethanol, dried at 60°C for 24 hours, and ground to obtain layered compound interlayer polyaniline or polypyrrole.
(3)氮掺杂类石墨烯催化剂的制备(3) Preparation of nitrogen-doped graphene-like catalyst
将步骤(2)所获得的层状化合物夹层聚苯胺或聚吡咯置于管式炉中,向管式炉中以流速为50~200毫升/分钟通入惰性气体0.5~1小时后,保持惰性气体流速,以6~20℃/分钟升温速度,先将管式炉升至120~180℃保持1~4小时,再继续升温至700~1000℃保持1~4小时,冷却至室温、研磨后,得到层状化合物夹层氮掺杂类石墨烯;按层状化合物∶氢氟酸质量比1∶2称取氢氟酸,其中氢氟酸质量浓度为40%;先将上述层状化合物夹层氮掺杂类石墨烯分散在乙醇中,超声搅拌3~8小时形成质量浓度为0.1~1克/毫升的层状化合物夹层氮掺杂类石墨烯悬浮液,再氢氟酸缓慢加入上述层状化合物夹层氮掺杂类石墨烯悬浮液中,超声搅拌反应10~20小时,最后经过滤,去离子水洗涤3次和无水乙醇洗涤3次,60℃干燥24小时,研磨后获得氮掺杂类石墨烯催化剂。The layered compound interlayer polyaniline or polypyrrole obtained in step (2) is placed in a tube furnace, and the inert gas is fed into the tube furnace at a flow rate of 50 to 200 ml/min for 0.5 to 1 hour, and then kept inert Gas flow rate, at a heating rate of 6-20°C/min, first raise the tube furnace to 120-180°C and keep it for 1-4 hours, then continue to heat up to 700-1000°C and keep it for 1-4 hours, cool to room temperature, and grind , obtain layered compound interlayer nitrogen-doped graphene; Press layered compound: hydrofluoric acid mass ratio 1: 2 takes hydrofluoric acid, wherein hydrofluoric acid mass concentration is 40%; First above-mentioned layered compound interlayer nitrogen Doped graphene is dispersed in ethanol, and ultrasonically stirred for 3 to 8 hours to form a layered compound interlayer nitrogen-doped graphene suspension with a mass concentration of 0.1 to 1 g/ml, and then hydrofluoric acid is slowly added to the layered compound In the interlayer nitrogen-doped graphene-like suspension, ultrasonically stirred and reacted for 10 to 20 hours, and finally filtered, washed with deionized water for 3 times and absolute ethanol for 3 times, dried at 60°C for 24 hours, and the nitrogen-doped graphene was obtained after grinding. Graphene catalyst.
其中所述层状化合物为蒙脱土、高岭土、水滑石和水镁石的其中之一,其中所述氧化剂为过硫酸铵、双氧水、高锰酸钾和氯化铁的其中之一;其中所述惰性气体为氮气和氩气的其中之一。Wherein the layered compound is one of montmorillonite, kaolin, hydrotalcite and brucite, wherein the oxidant is one of ammonium persulfate, hydrogen peroxide, potassium permanganate and ferric chloride; The inert gas is one of nitrogen and argon.
本发明采用上述技术方案后,主要有以下优点:After the present invention adopts above-mentioned technical scheme, mainly have the following advantages:
(1)催化剂具有良好的导电性、类似石墨烯的二维片层结构以及较高的石墨化程度,从而保证催化剂具有良好的稳定性。(1) The catalyst has good electrical conductivity, a two-dimensional sheet structure similar to graphene, and a high degree of graphitization, thereby ensuring good stability of the catalyst.
(2)氮掺杂效率高且可控制氮的化学态组成,使催化剂具有优异的氧还原催化性能。(2) The nitrogen doping efficiency is high and the chemical state composition of nitrogen can be controlled, so that the catalyst has excellent oxygen reduction catalytic performance.
(3)催化剂中并不存在任何形式的金属离子,催化剂在使用过程中不存在加速电解质膜降解的问题。(3) There are no metal ions in any form in the catalyst, and there is no problem of accelerating the degradation of the electrolyte membrane during the use of the catalyst.
本发明方法简单易行,生产成本低廉,采用本发明制备的氮掺杂类石墨烯催化剂具有优异的氧还原催活性、稳定性以及抗甲醇性。可应用于以质子交换膜为电解质的燃料电池,如氢氧质子交换膜燃料电池、直接甲醇燃料电池等的气体电极。用本发明制造的燃料电池,广泛应用于电动汽车,各种航天器,便携式电子设备,如摄像机,笔记本电脑,电动玩具等。The method of the invention is simple and easy, and the production cost is low. The nitrogen-doped graphene-like catalyst prepared by the invention has excellent oxygen reduction catalytic activity, stability and methanol resistance. It can be applied to fuel cells with proton exchange membrane as electrolyte, such as gas electrodes of hydrogen-oxygen proton exchange membrane fuel cells and direct methanol fuel cells. The fuel cell manufactured by the invention is widely used in electric automobiles, various spacecraft, portable electronic equipment, such as video cameras, notebook computers, electric toys and the like.
四、附图说明: 4. Description of drawings:
图1为实施例1所得氮掺杂类石墨烯催化剂和英国Jonhson-Matthey公司商业化Pt/C(铂质量百分比40%)催化剂在旋转圆盘电极上的氧还原线性扫描曲线。Fig. 1 is the oxygen reduction linear scan curve of the nitrogen-doped graphene-like catalyst obtained in Example 1 and the commercialized Pt/C (platinum mass percentage 40%) catalyst of British Jonhson-Matthey Company on the rotating disk electrode.
图中:曲线1是以实施例1制备的氮掺杂类石墨烯催化剂为工作电极,银/氯化银电极为参比电极,铂环为对电极,氧气饱和0.5摩尔/升硫酸水溶液为电解液,扫描速度为2毫伏/秒条件下的氧还原线性扫描曲线。Among the figure: curve 1 is that the nitrogen-doped graphene-like catalyst prepared in embodiment 1 is the working electrode, the silver/silver chloride electrode is the reference electrode, the platinum ring is the counter electrode, and the oxygen-saturated 0.5 mol/liter sulfuric acid aqueous solution is the electrolytic liquid, the oxygen reduction linear scan curve under the condition that the scan speed is 2 mV/s.
曲线2是英国Jonhson-Matthey公司商业化Pt/C(铂质量百分比40%)催化剂为工作电极,银/氯化银电极为参比电极,铂环为对电极,氧气饱和0.5摩尔/升硫酸水溶液为电解液,扫描速度为2毫伏/秒条件下的氧还原线性扫描曲线。
图2为实施例2制备的氮掺杂类石墨烯催化剂和英国Jonhson-Matthey公司商业化Pt/C(铂质量百分比40%)催化剂在旋转圆盘电极上的循环伏安曲线图。Fig. 2 is the cyclic voltammetry graph of the nitrogen-doped graphene-like catalyst prepared in Example 2 and the commercialized Pt/C (platinum mass percent 40%) catalyst of British Jonhson-Matthey Company on the rotating disk electrode.
图中:曲线1~2是以实施例2制备的氮掺杂类石墨烯催化剂为工作电极,银/氯化银电极为参比电极,铂环为对电极,氮气饱和0.5摩尔/升硫酸水溶液为电解液,扫描速度为50mV/s条件下的循环伏安曲线图。其中曲线1的扫描圈数为第1圈,曲线2的扫描圈数为第800圈。Among the figures: curves 1 to 2 are based on the nitrogen-doped graphene-like catalyst prepared in Example 2 as the working electrode, the silver/silver chloride electrode as the reference electrode, and the platinum ring as the counter electrode, nitrogen saturated with 0.5 mol/liter of sulfuric acid aqueous solution cyclic voltammetry curve under the conditions of electrolyte and scan speed of 50mV/s. Among them, the scanning circle number of curve 1 is the first circle, and the scanning circle number of
曲线3~4是英国Jonhson-Matthey公司商业化Pt/C(铂质量百分比40%)催化剂为工作电极,银/氯化银电极为参比电极,铂环为对电极,氮气饱和0.5摩尔/升硫酸水溶液为电解液,扫描速度为50mV/s条件下的循环伏安曲线图。其中曲线3的扫描圈数为第1圈,曲线4的扫描圈数为第800圈。
图3为实施例3所制备的氮掺杂类石墨烯催化剂老化前后的氧还原线性扫描曲线。Fig. 3 is the oxygen reduction linear scan curve before and after aging of the nitrogen-doped graphene-like catalyst prepared in Example 3.
图中:曲线1是以实施例3制备的氮掺杂类石墨烯催化剂老化前的催化氧还原线性扫描曲线。In the figure: Curve 1 is the catalytic oxygen reduction linear scanning curve of the nitrogen-doped graphene-like catalyst prepared in Example 3 before aging.
曲线2是以实施例3制备的氮掺杂类石墨烯催化剂老化后的催化氧还原线性扫描曲线。
图4为实施例4制备的氮掺杂类石墨烯催化剂放大倍数为50000倍时的扫描电子显微镜图。FIG. 4 is a scanning electron microscope image of the nitrogen-doped graphene-like catalyst prepared in Example 4 at a magnification of 50,000 times.
图5为实施例1制备的氮掺杂类石墨烯催化剂为阴极氧还原催化剂的质子交换膜氢氧燃料电池单电池测试曲线。Fig. 5 is a test curve of a proton exchange membrane hydrogen-oxygen fuel cell single cell in which the nitrogen-doped graphene-like catalyst prepared in Example 1 is used as the cathode oxygen reduction catalyst.
图中:曲线1是以实施例1制备的氮掺杂类石墨烯催化剂为燃料电池阴极催化剂的功率曲线,曲线2是以实施例1制备的氮掺杂类石墨烯催化剂为燃料电池阴极催化剂的极化曲线。Among the figure: Curve 1 is the power curve of the fuel cell cathode catalyst based on the nitrogen-doped graphene-like catalyst prepared in Example 1, and
五、具体实施方式: 5. Specific implementation methods:
下面结合具体实施方式,进一步说明本发明。The present invention will be further described below in combination with specific embodiments.
实施例1Example 1
一种氧还原非贵金属催化剂及其制备方法,其具体方法步骤包括:An oxygen-reducing non-noble metal catalyst and a preparation method thereof, the specific method steps comprising:
(1)苯胺插层的蒙脱土悬浮液制备(1) Preparation of montmorillonite suspension for aniline intercalation
按蒙脱土∶苯胺的质量比为1∶1称取蒙脱土和苯胺,先将蒙脱土分散在去离子水中,超声搅拌5小时形成质量浓度为0.05克/毫升的蒙脱土悬浮液;按蒙脱土悬浮液∶乙醇的体积比为1∶0.5量取乙醇,将苯胺溶于乙醇中,并加入到上述蒙脱土悬浮液中,20℃搅拌30小时,形成苯胺插层的蒙脱土悬浮液。Weigh montmorillonite and aniline according to the mass ratio of montmorillonite: aniline of 1:1, first disperse montmorillonite in deionized water, and ultrasonically stir for 5 hours to form a montmorillonite suspension with a mass concentration of 0.05 g/ml Measure ethanol by montmorillonite suspension: the volume ratio of ethanol is 1: 0.5, dissolve aniline in ethanol, and join in the above-mentioned montmorillonite suspension, stir 30 hours at 20 ℃, form the montmorillonite intercalation of aniline Desoil suspension.
(2)苯胺层间聚合(2) Interlayer polymerization of aniline
按步骤(1)所获得的苯胺插层的蒙脱土悬浮液∶硫酸溶液的体积比1∶0.3量取硫酸溶液,其中硫酸溶液浓度为1摩尔/升;按苯胺∶过硫酸铵的质量比为1∶1称取过硫酸铵,并溶于去离子水中形成质量浓度为0.5克/毫升过硫酸铵溶液;先将硫酸溶液加入到步骤(1)所获得的苯胺插层的蒙脱土悬浮液中,搅拌2小时,再将过硫酸铵溶液以0.5毫升/分钟速度加入上述悬浮液中,5℃搅拌反应20小时,最后经真空抽滤,去离子水洗涤3次和无水乙醇洗涤3次,60℃干燥24小时,研磨后获得蒙脱土夹层聚苯胺。The montmorillonite suspension of the aniline intercalation obtained by step (1): the volume ratio of sulfuric acid solution 1: 0.3 measures sulfuric acid solution, wherein the concentration of sulfuric acid solution is 1 mole/liter; by aniline: the mass ratio of ammonium persulfate Ammonium persulfate is weighed at 1:1, and dissolved in deionized water to form a mass concentration of 0.5 g/ml ammonium persulfate solution; the sulfuric acid solution is first added to the aniline intercalated montmorillonite suspension obtained in step (1) solution, stirred for 2 hours, then ammonium persulfate solution was added to the above suspension at a rate of 0.5 ml/min, stirred and reacted at 5°C for 20 hours, and finally vacuum filtered, washed with deionized water for 3 times and absolute ethanol for 3 times Once, dry at 60°C for 24 hours and grind to obtain polyaniline interlayered with montmorillonite.
(3)氮掺杂类石墨烯催化剂的制备(3) Preparation of nitrogen-doped graphene-like catalyst
将步骤(2)所获得的蒙脱土夹层聚苯胺置于管式炉中,向管式炉中以流速为100毫升/分钟通入氮气0.8小时后,保持氮气流速,以10℃/分钟升温速度,先将管式炉升至150℃保持3小时,再继续升温至900℃保持3小时,冷却至室温、研磨后,得到蒙脱土夹层氮掺杂类石墨烯;按蒙脱土∶氢氟酸质量比1∶2称取氢氟酸,其中氢氟酸质量浓度为40%;先将上述蒙脱土夹层氮掺杂类石墨烯分散在乙醇中,超声搅拌5小时形成质量浓度为0.5克/毫升的蒙脱土夹层氮掺杂类石墨烯悬浮液,再氢氟酸缓慢加入上述蒙脱土夹层氮掺杂类石墨烯悬浮液中,超声搅拌反应15小时,最后经过滤,去离子水洗涤3次和无水乙醇洗涤3次,60℃干燥24小时,研磨后获得氮掺杂类石墨烯催化剂。The montmorillonite interlayer polyaniline obtained in step (2) is placed in a tube furnace, and after 0.8 hours of nitrogen gas is passed into the tube furnace with a flow rate of 100 ml/min, the nitrogen flow rate is maintained and the temperature is raised at 10° C./min. Speed, first raise the tube furnace to 150°C for 3 hours, then continue to heat up to 900°C for 3 hours, cool to room temperature, and grind to obtain montmorillonite interlayer nitrogen-doped graphene; according to montmorillonite: hydrogen Hydrofluoric acid mass ratio 1:2 Weigh hydrofluoric acid, wherein the mass concentration of hydrofluoric acid is 40%; first disperse the above-mentioned montmorillonite interlayer nitrogen-doped graphene in ethanol, and ultrasonically stir for 5 hours to form a mass concentration of 0.5% gram/milliliter montmorillonite interlayer nitrogen-doped graphene-like suspension, then slowly add hydrofluoric acid into the above-mentioned montmorillonite interlayer nitrogen-doped graphene-like suspension, ultrasonically stir for 15 hours, and finally filter and deionize Washing with water for 3 times and absolute ethanol for 3 times, drying at 60° C. for 24 hours, and grinding to obtain a nitrogen-doped graphene-like catalyst.
(4)氮掺杂类石墨烯催化剂的氧还原测试(4) Oxygen reduction test of nitrogen-doped graphene-like catalyst
称取2毫克第(3)步所制得的氮掺杂类石墨烯催化剂加入到200微升无水乙醇溶液中超声振荡10分钟分散均匀后,微量进样器吸取5微升滴于玻璃碳旋转圆盘电极上,60℃干燥后,再吸取5微升0.05%Nafion溶液滴于催化层上,60℃下保持2小时。以此电极为工作电极,铂环电极和银/氯化银电极(Ag/AgCl)电极分别作为辅助电极和参比电极,在氧气气饱和0.5mol/L的硫酸溶液中测试氧还原线性扫描曲线。扫描速率为2mV/s,扫描范围为0.9~0V(vs.Ag/AgCl),测试结果如图1曲线1所示。Weigh 2 mg of the nitrogen-doped graphene-like catalyst prepared in step (3) and add it to 200 microliters of absolute ethanol solution and ultrasonically oscillate for 10 minutes to disperse evenly. After drying at 60°C on the rotating disc electrode, pipette 5 microliters of 0.05% Nafion solution and drop it on the catalytic layer, and keep it at 60°C for 2 hours. Use this electrode as the working electrode, the platinum ring electrode and the silver/silver chloride electrode (Ag/AgCl) electrode as the auxiliary electrode and the reference electrode respectively, and measure the linear scan curve of oxygen reduction in a sulfuric acid solution saturated with oxygen at 0.5mol/L . The scan rate is 2mV/s, and the scan range is 0.9-0V (vs.Ag/AgCl). The test results are shown in curve 1 in Figure 1.
(5)氮掺杂类石墨烯催化剂质子交换膜燃料电池电极的单电池性能评价(5) Single-cell performance evaluation of nitrogen-doped graphene-like catalyst proton exchange membrane fuel cell electrode
以第(3)步制备的氮掺杂类石墨烯催化剂电极为质子交换膜燃料电池阴极,催化剂载量为3.7mg/cm2,传统Pt/C气体多孔电极为阳极。将Nafion112膜置于阳极和阴极之间,在137℃和5兆帕压力下热压120秒后,取出冷却至室温,制得燃料电池的“膜电极”组件。然后将“膜电极”组件装入燃料电池夹具进行评价。以纯氢为燃料,纯氧为氧化剂,电池测试温度80℃,正负极背压均为200千帕(绝对压力),负极氢气流速180-200毫升/分钟,正极O2流速200-300毫升/分钟。The nitrogen-doped graphene-like catalyst electrode prepared in step (3) was used as the cathode of the proton exchange membrane fuel cell, and the catalyst loading was 3.7 mg/cm 2 , and the traditional Pt/C gas porous electrode was used as the anode. The Nafion112 membrane was placed between the anode and the cathode, and after hot pressing at 137°C and 5 MPa pressure for 120 seconds, it was taken out and cooled to room temperature to obtain the "membrane electrode" assembly of the fuel cell. The "membrane electrode" assembly was then loaded into a fuel cell fixture for evaluation. Using pure hydrogen as fuel and pure oxygen as oxidant, the battery test temperature is 80°C, the positive and negative electrode back pressures are both 200 kPa (absolute pressure), the negative electrode hydrogen flow rate is 180-200 ml/min, and the positive electrode O2 flow rate is 200-300 ml/min minute.
单电池极化曲线在恒电位条件下测试,记录电位随电流密度的变化情况,对应图5中曲线2。记录功率密度随电流密度的变化情况,对应图5中曲线1。The polarization curve of the single cell was tested under constant potential conditions, and the variation of the potential with the current density was recorded, corresponding to
实施例2Example 2
一种氧还原非贵金属催化剂及其制备方法,其具体方法步骤包括:An oxygen-reducing non-noble metal catalyst and a preparation method thereof, the specific method steps comprising:
(1)吡咯插层的高岭土悬浮液制备(1) Preparation of kaolin suspension for pyrrole intercalation
按高岭土∶吡咯的质量比为1∶4称取高岭土和吡咯,先将高岭土分散在去离子水中,超声搅拌8小时形成质量浓度为0.1克/毫升的高岭土悬浮液;按高岭土悬浮液∶丙酮的体积比为1∶1量取丙酮,将吡咯溶于丙酮中,并加入到上述高岭土悬浮液中,60℃搅拌10小时,形成吡咯插层的高岭土悬浮液。It is 1: 4 to weigh kaolin and pyrrole by kaolin: the mass ratio of pyrrole, first kaolin is dispersed in deionized water, and ultrasonic stirring 8 hours forms the kaolin suspension that mass concentration is 0.1 g/ml; Press kaolin suspension: acetone Acetone was measured at a volume ratio of 1:1, pyrrole was dissolved in acetone, and added to the above kaolin suspension, stirred at 60°C for 10 hours to form a pyrrole-intercalated kaolin suspension.
(2)吡咯层间聚合(2) Interlayer polymerization of pyrrole
按步骤(1)所获得的吡咯插层的高岭土悬浮液∶盐酸溶液的体积比1∶0.5量取盐酸溶液,其中盐酸溶液浓度为0.5摩尔/升;按吡咯∶双氧水的质量比为1∶2称取双氧水,并溶于去离子水中形成质量浓度为1克/毫升双氧水溶液;先将盐酸溶液加入到步骤(1)所获得的吡咯插层的高岭土悬浮液中,搅拌3小时,再将双氧水溶液以1毫升/分钟速度加入上述悬浮液中,10℃搅拌反应30小时,最后经真空抽滤,去离子水洗涤3次和无水乙醇洗涤3次,60℃干燥24小时,研磨后获得高岭土夹层聚吡咯。The kaolin suspension of pyrrole intercalation obtained by step (1): the volume ratio of hydrochloric acid solution 1: 0.5 measures hydrochloric acid solution, wherein the concentration of hydrochloric acid solution is 0.5 mole/liter; by pyrrole: the mass ratio of hydrogen peroxide is 1: 2 Weigh hydrogen peroxide, and dissolve it in deionized water to form a hydrogen peroxide solution with a mass concentration of 1 g/ml; first add the hydrochloric acid solution to the pyrrole-intercalated kaolin suspension obtained in step (1), stir for 3 hours, and then add the hydrogen peroxide The solution was added to the above suspension at a speed of 1 ml/min, stirred and reacted at 10°C for 30 hours, finally vacuum filtered, washed with deionized water and absolute ethanol for 3 times, dried at 60°C for 24 hours, and kaolin was obtained after grinding Interlayer polypyrrole.
(3)氮掺杂类石墨烯催化剂的制备(3) Preparation of nitrogen-doped graphene-like catalyst
将步骤(2)所获得的高岭土夹层聚吡咯置于管式炉中,向管式炉中以流速为200毫升/分钟通入氩气0.5小时后,保持氩气流速,以20℃/分钟升温速度,先将管式炉升至180℃保持4小时,再继续升温至1000℃保持1小时,冷却至室温、研磨后,得到高岭土夹层氮掺杂类石墨烯;按高岭土∶氢氟酸质量比1∶2称取氢氟酸,其中氢氟酸质量浓度为40%;先将上述高岭土夹层氮掺杂类石墨烯分散在乙醇中,超声搅拌8小时形成质量浓度为1克/毫升的高岭土夹层氮掺杂类石墨烯悬浮液,再氢氟酸缓慢加入上述高岭土夹层氮掺杂类石墨烯悬浮液中,超声搅拌反应20小时,最后经过滤,去离子水洗涤3次和无水乙醇洗涤3次,60℃干燥24小时,研磨后获得氮掺杂类石墨烯催化剂。The kaolin interlayer polypyrrole obtained in step (2) is placed in a tube furnace, and after 0.5 hours of passing argon gas into the tube furnace with a flow rate of 200 ml/min, the argon flow rate is maintained and the temperature is raised at 20° C./min. Speed, first raise the tube furnace to 180°C for 4 hours, then continue to heat up to 1000°C for 1 hour, cool to room temperature, and grind to obtain kaolin interlayer nitrogen-doped graphene; according to the mass ratio of kaolin: hydrofluoric acid Weigh hydrofluoric acid at 1:2, wherein the mass concentration of hydrofluoric acid is 40%; first disperse the above-mentioned kaolin interlayer nitrogen-doped graphene in ethanol, and ultrasonically stir for 8 hours to form a kaolin interlayer with a mass concentration of 1 g/ml Nitrogen-doped graphene-like suspension, hydrofluoric acid is slowly added to the above-mentioned kaolin interlayer nitrogen-doped graphene-like suspension, ultrasonically stirred for 20 hours, finally filtered, washed with deionized water for 3 times and absolute ethanol for 3 times Once, dry at 60°C for 24 hours, and grind to obtain a nitrogen-doped graphene-like catalyst.
(4)氮掺杂类石墨烯催化剂的稳定性测试(4) Stability test of nitrogen-doped graphene-like catalyst
称取2毫克第(3)步所制得的氮掺杂类石墨烯催化剂加入到200微升无水乙醇溶液中超声振荡10分钟分散均匀后,微量进样器吸取5微升滴于玻璃碳旋转圆盘电极上,60℃干燥后,再吸取5微升0.05%Nafion溶液滴于催化层上,60℃下保持2小时。以此电极为工作电极,铂环电极和银/氯化银电极(Ag/AgCl)电极分别作为辅助电极和参比电极,在氮气饱和0.5mol/L的硫酸溶液中测试循环伏安曲线。扫描速率为50mV/s,扫描范围为-0.2~0.8V(vs.Ag/AgCl),共计扫描800圈。测试结果如图2曲线1~2所示。Weigh 2 mg of the nitrogen-doped graphene-like catalyst prepared in step (3) and add it to 200 microliters of absolute ethanol solution and ultrasonically oscillate for 10 minutes to disperse evenly. After drying at 60°C on the rotating disc electrode, pipette 5 microliters of 0.05% Nafion solution and drop it on the catalytic layer, and keep it at 60°C for 2 hours. Using this electrode as the working electrode, the platinum ring electrode and the silver/silver chloride electrode (Ag/AgCl) electrode as the auxiliary electrode and the reference electrode, respectively, the cyclic voltammetry curve was tested in a sulfuric acid solution saturated with nitrogen at 0.5 mol/L. The scanning rate is 50mV/s, the scanning range is -0.2~0.8V (vs.Ag/AgCl), and a total of 800 cycles are scanned. The test results are shown in curves 1-2 in Figure 2.
实施例3Example 3
一种氧还原非贵金属催化剂及其制备方法,其具体方法步骤包括:An oxygen-reducing non-noble metal catalyst and a preparation method thereof, the specific method steps comprising:
(1)苯胺插层的水滑石悬浮液制备(1) Preparation of hydrotalcite suspension for aniline intercalation
按水滑石∶苯胺的质量比为1∶0.1称取水滑石和苯胺,先将水滑石分散在去离子水中,超声搅拌3小时形成质量浓度为0.01克/毫升的水滑石悬浮液;按水滑石悬浮液∶乙腈的体积比为1∶0.3量取乙腈,将苯胺溶于乙腈中,并加入到上述水滑石悬浮液中,10℃搅拌40小时,形成苯胺插层的水滑石悬浮液。Weigh hydrotalcite and aniline according to the mass ratio of hydrotalcite: aniline of 1:0.1, first disperse the hydrotalcite in deionized water, and stir ultrasonically for 3 hours to form a hydrotalcite suspension with a mass concentration of 0.01 g/ml; The volume ratio of liquid: acetonitrile is 1:0.3. Measure acetonitrile, dissolve aniline in acetonitrile, and add it to the above hydrotalcite suspension, stir at 10°C for 40 hours to form an aniline-intercalated hydrotalcite suspension.
(2)苯胺层间聚合(2) Interlayer polymerization of aniline
按步骤(1)所获得的苯胺插层的水滑石悬浮液∶硫酸溶液的体积比1∶0.1量取硫酸溶液,其中硫酸溶液浓度为1.5摩尔/升;按苯胺∶高锰酸钾的质量比为1∶0.5称取高锰酸钾,并溶于去离子水中形成质量浓度为0.1克/毫升高锰酸钾溶液;先将硫酸溶液加入到步骤(1)所获得的苯胺插层的水滑石悬浮液中,搅拌1小时,再将高锰酸钾溶液以0.1毫升/分钟速度加入上述悬浮液中,0℃搅拌反应10小时,最后经真空抽滤,去离子水洗涤3次和无水乙醇洗涤3次,60℃干燥24小时,研磨后获得水滑石夹层聚苯胺。The hydrotalcite suspension of the aniline intercalation obtained by step (1): the volume ratio of sulfuric acid solution 1: 0.1 measures sulfuric acid solution, wherein the concentration of sulfuric acid solution is 1.5 mol/liter; by aniline: the mass ratio of potassium permanganate Potassium permanganate is weighed at 1:0.5, and dissolved in deionized water to form a mass concentration of 0.1 g/ml potassium permanganate solution; the sulfuric acid solution is first added to the hydrotalcite intercalated with aniline obtained in step (1) In the suspension, stir for 1 hour, then add potassium permanganate solution to the above suspension at a rate of 0.1 ml/min, stir and react at 0°C for 10 hours, and finally vacuum filter, wash with
(3)氮掺杂类石墨烯催化剂的制备(3) Preparation of nitrogen-doped graphene-like catalyst
将步骤(2)所获得的水滑石夹层聚苯胺置于管式炉中,向管式炉中以流速为50毫升/分钟通入氮气1小时后,保持氮气流速,以6℃/分钟升温速度,先将管式炉升至120℃保持1小时,再继续升温至700℃保持4小时,冷却至室温、研磨后,得到水滑石夹层氮掺杂类石墨烯;按水滑石∶氢氟酸质量比1∶2称取氢氟酸,其中氢氟酸质量浓度为40%;先将上述水滑石夹层氮掺杂类石墨烯分散在乙醇中,超声搅拌3小时形成质量浓度为0.1克/毫升的水滑石夹层氮掺杂类石墨烯悬浮液,再氢氟酸缓慢加入上述水滑石夹层氮掺杂类石墨烯悬浮液中,超声搅拌反应10小时,最后经过滤,去离子水洗涤3次和无水乙醇洗涤3次,60℃干燥24小时,研磨后获得氮掺杂类石墨烯催化剂。The hydrotalcite interlayer polyaniline obtained in step (2) is placed in a tube furnace, and after nitrogen is passed into the tube furnace with a flow rate of 50 ml/min for 1 hour, the nitrogen flow rate is maintained, and the temperature rise rate is 6° C./min. First, the tube furnace is raised to 120°C for 1 hour, and then continues to heat up to 700°C for 4 hours. After cooling to room temperature and grinding, a hydrotalcite interlayer nitrogen-doped graphene is obtained; according to the hydrotalcite: hydrofluoric acid mass Weigh hydrofluoric acid at a ratio of 1:2, wherein the mass concentration of hydrofluoric acid is 40%; first disperse the above-mentioned hydrotalcite interlayer nitrogen-doped graphene in ethanol, and ultrasonically stir for 3 hours to form a mass concentration of 0.1 g/ml Hydrotalcite interlayer nitrogen-doped graphene-like suspension, then slowly add hydrofluoric acid into the above-mentioned hydrotalcite interlayer nitrogen-doped graphene-like suspension, ultrasonically stir and react for 10 hours, finally filter, wash with deionized water for 3 times and remove Washed with water and ethanol three times, dried at 60°C for 24 hours, and ground to obtain a nitrogen-doped graphene-like catalyst.
(4)氮掺杂类石墨烯催化剂的老化前后氧还原测试(4) Oxygen reduction test before and after aging of nitrogen-doped graphene-like catalyst
称取2毫克第(3)步所制得的氮掺杂类石墨烯催化剂加入到200微升无水乙醇溶液中超声振荡10分钟分散均匀后,微量进样器吸取5微升滴于玻璃碳旋转圆盘电极上,60℃干燥后,再吸取5微升0.05%Nafion溶液滴于催化层上,60℃下保持2小时。以此电极为工作电极,铂环电极和银/氯化银电极(Ag/AgCl)电极分别作为辅助电极和参比电极,在氧气气饱和0.5mol/L的硫酸溶液中测试老化前氧还原线性扫描曲线。扫描速率为2mV/s,扫描范围为0.9~0V(vs.Ag/AgCl),测试结果如图3曲线1所示。此电极在氮气饱和的0.5mol/L的硫酸溶液中进行循环伏安老化800圈后,再次在氧气气饱和0.5mol/L的硫酸溶液中测试老化后氧还原线性扫描曲线,测试结构如图3曲线2所示。Weigh 2 mg of the nitrogen-doped graphene-like catalyst prepared in step (3) and add it to 200 microliters of absolute ethanol solution and ultrasonically oscillate for 10 minutes to disperse evenly. After drying at 60°C on the rotating disc electrode, pipette 5 microliters of 0.05% Nafion solution and drop it on the catalytic layer, and keep it at 60°C for 2 hours. This electrode is used as the working electrode, the platinum ring electrode and the silver/silver chloride electrode (Ag/AgCl) electrode are used as the auxiliary electrode and the reference electrode respectively, and the oxygen reduction linearity before aging is tested in a sulfuric acid solution saturated with oxygen at 0.5mol/L. Scan curve. The scan rate is 2mV/s, and the scan range is 0.9-0V (vs.Ag/AgCl). The test results are shown in curve 1 in Figure 3. After cyclic voltammetric aging of the electrode for 800 cycles in a nitrogen-saturated 0.5mol/L sulfuric acid solution, the oxygen reduction linear scan curve after aging was tested again in an oxygen-saturated 0.5mol/L sulfuric acid solution. The test structure is shown in Figure 3
实施例4Example 4
一种氧还原非贵金属催化剂及其制备方法,其具体方法步骤包括:An oxygen-reducing non-noble metal catalyst and a preparation method thereof, the specific method steps comprising:
(1)吡咯插层的水镁石悬浮液制备(1) Preparation of brucite suspension for pyrrole intercalation
按水镁石∶吡咯的质量比为1∶3称取水镁石和吡咯,先将水镁石分散在去离子水中,超声搅拌6小时形成质量浓度为0.8克/毫升的水镁石悬浮液;按水镁石悬浮液∶乙醇的体积比为1∶0.6量取乙醇,将吡咯溶于乙醇中,并加入到上述水镁石悬浮液中,35℃搅拌25小时,形成吡咯插层的水镁石悬浮液。According to brucite: the mass ratio of pyrrole is 1: 3 to take brucite and pyrrole, first brucite is dispersed in deionized water, and ultrasonic stirring is formed for 6 hours to form a mass concentration of brucite suspension of 0.8 g/ml; The volume ratio of brucite suspension: ethanol is 1:0.6. Measure ethanol, dissolve pyrrole in ethanol, and add it to the above-mentioned brucite suspension, stir at 35°C for 25 hours to form pyrrole-intercalated brucite suspension.
(2)吡咯层间聚合(2) Interlayer polymerization of pyrrole
按步骤(1)所获得的吡咯插层的水镁石悬浮液∶盐酸溶液的体积比1∶0.4量取盐酸溶液,其中盐酸溶液浓度为0.8摩尔/升;按吡咯∶氯化铁的质量比为1∶1.5称取氯化铁,并溶于去离子水中形成质量浓度为0.8克/毫升氯化铁溶液;先将盐酸溶液加入到步骤(1)所获得的吡咯插层的水镁石悬浮液中,搅拌2.5小时,再将氯化铁溶液以0.6毫升/分钟速度加入上述悬浮液中,8℃搅拌反应25小时,最后经真空抽滤,去离子水洗涤3次和无水乙醇洗涤3次,60℃干燥24小时,研磨后获得水镁石夹层聚吡咯。The brucite suspension of pyrrole intercalation obtained by step (1): the volume ratio of hydrochloric acid solution 1: 0.4 measures hydrochloric acid solution, wherein the concentration of hydrochloric acid solution is 0.8 mole/liter; by pyrrole: the mass ratio of ferric chloride Ferric chloride is weighed as 1: 1.5, and dissolved in deionized water to form a mass concentration of 0.8 g/ml ferric chloride solution; first the hydrochloric acid solution is added to the pyrrole-intercalated brucite suspension obtained in step (1) solution, stirred for 2.5 hours, then ferric chloride solution was added to the above suspension at a rate of 0.6 ml/min, stirred and reacted at 8°C for 25 hours, and finally vacuum filtered, washed with deionized water for 3 times and absolute ethanol for 3 times Once, dry at 60°C for 24 hours and grind to obtain brucite interlayer polypyrrole.
(3)氮掺杂类石墨烯催化剂的制备(3) Preparation of nitrogen-doped graphene-like catalyst
将步骤(2)所获得的水镁石夹层聚吡咯置于管式炉中,向管式炉中以流速为120毫升/分钟通入氩气0.8小时后,保持氩气流速,以15℃/分钟升温速度,先将管式炉升至150℃保持2小时,再继续升温至800℃保持2小时,冷却至室温、研磨后,得到水镁石夹层氮掺杂类石墨烯;按水镁石∶氢氟酸质量比1∶2称取氢氟酸,其中氢氟酸质量浓度为40%;先将上述水镁石夹层氮掺杂类石墨烯分散在乙醇中,超声搅拌5小时形成质量浓度为0.6克/毫升的水镁石夹层氮掺杂类石墨烯悬浮液,再氢氟酸缓慢加入上述水镁石夹层氮掺杂类石墨烯悬浮液中,超声搅拌反应12小时,最后经过滤,去离子水洗涤3次和无水乙醇洗涤3次,60℃干燥24小时,研磨后获得氮掺杂类石墨烯催化剂。The brucite interlayer polypyrrole obtained in step (2) is placed in a tube furnace, and after 0.8 hours of passing argon gas into the tube furnace with a flow rate of 120 ml/min, the argon flow rate is maintained at 15° C./min. Minute heating rate, first raise the tube furnace to 150°C for 2 hours, then continue to heat up to 800°C for 2 hours, cool to room temperature, and grind to obtain brucite interlayer nitrogen-doped graphene; according to brucite : Hydrofluoric acid mass ratio 1: 2 takes hydrofluoric acid, wherein hydrofluoric acid mass concentration is 40%; First above-mentioned brucite interlayer nitrogen-doped graphene is dispersed in ethanol, and ultrasonic stirring forms mass concentration in 5 hours 0.6 g/ml brucite interlayer nitrogen-doped graphene-like suspension, then hydrofluoric acid is slowly added to the above-mentioned brucite interlayer nitrogen-doped graphene-like suspension, ultrasonically stirred for 12 hours, and finally filtered, Washing with deionized water for 3 times and absolute ethanol for 3 times, drying at 60°C for 24 hours, and grinding to obtain a nitrogen-doped graphene-like catalyst.
制备好的氮掺杂类石墨烯催化剂用扫描电镜测试得到图4中的扫描电镜(SEM)照片。The prepared nitrogen-doped graphene-like catalyst was tested with a scanning electron microscope to obtain a scanning electron microscope (SEM) photo in FIG. 4 .
对比实验Comparative Experiment
英国Jonhson-Matthey公司商业化Pt/C(铂质量百分比40%)催化剂的氧还原线性扫描曲线测试同实施例1中步骤(4),氧还原线性扫描曲线如图1中的曲线2所示;稳定性测试同实施例2中步骤(4),如图2曲线3~4所示。The oxygen reduction linear sweep curve test of the commercialized Pt/C (platinum mass percent 40%) catalyst of British Johnson-Matthey company is the same as step (4) in Example 1, and the oxygen reduction linear sweep curve is as shown in
本发明的试验结果:Test result of the present invention:
从图1中的氧还原曲线表明氮掺杂类石墨烯催化剂显示出了优异的氧还原催化性能,催化氧还原的半波电位与Jonhson-Matthey公司商业化Pt/C催化剂仅相差50mV。图2可以看出,在循环伏案扫描800圈后,采用本发明所制得的氮掺杂类石墨烯催化剂的循环伏案曲线(图2曲线1~2)基本没有变化,而英国Jonhson-Matthey公司商业化Pt/C催化剂的氢吸/脱附区面积(图2曲线3~4)却有了非常明显的减小,这表明氮掺杂类石墨烯催化剂稳定性显著且优于商业化Pt/C催化剂。从图3中可以看出,氮掺杂类石墨烯催化剂在循环伏案老化前后催化氧还原活性无明显改变,说明氮掺杂类石墨烯催化剂具有优异的催化氧还原稳定性。图4中的氮掺杂类石墨烯催化剂具有与石墨烯相似的纳米片层结构。图5中可以看出,以氮掺杂类石墨烯催化剂为阴极催化剂时单电池最大功率可达263mW/cm2。The oxygen reduction curve in Figure 1 shows that the nitrogen-doped graphene-like catalyst exhibits excellent oxygen reduction catalytic performance, and the half-wave potential of the catalytic oxygen reduction is only 50mV away from the commercial Pt/C catalyst of Jonhson-Matthey Company. As can be seen from Fig. 2, after cyclic desk scanning 800 circles, the cyclic desk curve (Fig. 2 curve 1~2) of the nitrogen-doped graphene-like catalyst prepared by the present invention does not change substantially, while British Jonhson-Matthey company The hydrogen absorption/desorption area of the commercial Pt/C catalyst (curve 3-4 in Figure 2) has been significantly reduced, which indicates that the nitrogen-doped graphene-like catalyst is significantly more stable than the commercial Pt/C catalyst. C catalyst. It can be seen from Figure 3 that the catalytic oxygen reduction activity of the nitrogen-doped graphene-like catalyst has no significant change before and after cyclic desk aging, indicating that the nitrogen-doped graphene-like catalyst has excellent catalytic oxygen reduction stability. The nitrogen-doped graphene-like catalyst in Figure 4 has a nanosheet structure similar to graphene. It can be seen from Fig. 5 that when the nitrogen-doped graphene-like catalyst is used as the cathode catalyst, the maximum power of the single cell can reach 263mW/cm 2 .
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| CN103769072A (en) * | 2012-10-18 | 2014-05-07 | 湘潭大学 | Titanium dioxide nano-tube-carbon composite material and preparation method and purpose thereof |
| CN103920519A (en) * | 2014-04-23 | 2014-07-16 | 西南大学 | Preparation method of oxygen reduction electro-catalyst based on iron-tungsten double-metal oxide enhanced nitrogen-doped graphene |
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| CN103769072B (en) * | 2012-10-18 | 2015-12-16 | 湘潭大学 | Titania nanotube-carbon composite and its production and use |
| CN103769072A (en) * | 2012-10-18 | 2014-05-07 | 湘潭大学 | Titanium dioxide nano-tube-carbon composite material and preparation method and purpose thereof |
| CN104107729B (en) * | 2013-04-16 | 2017-03-15 | 中国石油化工股份有限公司 | The renovation process of epoxidation catalyst |
| CN104107729A (en) * | 2013-04-16 | 2014-10-22 | 中国石油化工股份有限公司 | Method for regenerating epoxidation catalyst |
| CN104117356A (en) * | 2013-04-26 | 2014-10-29 | 中国科学院大连化学物理研究所 | Preparation method of non-noble metal catalyst used for oxygen reduction reaction |
| CN104117356B (en) * | 2013-04-26 | 2017-04-12 | 中国科学院大连化学物理研究所 | Preparation method of non-noble metal catalyst used for oxygen reduction reaction |
| CN103920519A (en) * | 2014-04-23 | 2014-07-16 | 西南大学 | Preparation method of oxygen reduction electro-catalyst based on iron-tungsten double-metal oxide enhanced nitrogen-doped graphene |
| CN103972516A (en) * | 2014-05-22 | 2014-08-06 | 胡国良 | Preparation method of carbon-supported alloy electrode of fuel cell |
| CN104058385A (en) * | 2014-06-13 | 2014-09-24 | 重庆大学 | Method for preparing functional carbon material in salt recrystallization solid mode |
| CN105060282A (en) * | 2015-08-05 | 2015-11-18 | 常州市长润石油有限公司 | Method for preparing sulfur-doped graphene from waste lubricating oil regeneration production waste water |
| CN105720276B (en) * | 2016-03-07 | 2018-08-31 | 昆明理工大学 | A method for preparing high-performance carbon-based catalysts |
| CN108428904A (en) * | 2018-04-04 | 2018-08-21 | 北京航空航天大学 | One kind hydrotalcite oxygen reduction catalyst of silver-based containing cerium and the preparation method and application thereof |
| CN108428904B (en) * | 2018-04-04 | 2020-05-08 | 北京航空航天大学 | A kind of cerium-containing silver-based hydrotalcite oxygen reduction catalyst and preparation method and application thereof |
| CN109301223A (en) * | 2018-10-12 | 2019-02-01 | 中南大学 | Lithium-sulfur battery cathode composite material and preparation method thereof |
| CN109461909A (en) * | 2018-10-12 | 2019-03-12 | 中南大学 | Lithium sulfur battery anode material and preparation method thereof |
| CN109301223B (en) * | 2018-10-12 | 2021-09-03 | 中南大学 | Lithium-sulfur battery positive electrode composite material and preparation method thereof |
| CN112125334A (en) * | 2019-06-24 | 2020-12-25 | 厦门稀土材料研究所 | A metal oxide/carbon intercalated two-dimensional composite material and its preparation method and application |
| CN113173570A (en) * | 2021-04-21 | 2021-07-27 | 国网黑龙江省电力有限公司电力科学研究院 | Preparation method and application of graphene-like sheet nitrogen-doped porous carbon material |
| CN113173570B (en) * | 2021-04-21 | 2022-12-09 | 国网黑龙江省电力有限公司电力科学研究院 | Preparation method and application of a graphene-like sheet-like nitrogen-doped porous carbon material |
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