CN113285080B - Nitrogen-phosphorus co-doped FeW/N, P-C composite material derived from phytic acid and preparation and application thereof - Google Patents
Nitrogen-phosphorus co-doped FeW/N, P-C composite material derived from phytic acid and preparation and application thereof Download PDFInfo
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- 239000002131 composite material Substances 0.000 title claims abstract description 67
- 229910052757 nitrogen Inorganic materials 0.000 title claims abstract description 58
- IMQLKJBTEOYOSI-GPIVLXJGSA-N Inositol-hexakisphosphate Chemical compound OP(O)(=O)O[C@H]1[C@H](OP(O)(O)=O)[C@@H](OP(O)(O)=O)[C@H](OP(O)(O)=O)[C@H](OP(O)(O)=O)[C@@H]1OP(O)(O)=O IMQLKJBTEOYOSI-GPIVLXJGSA-N 0.000 title claims abstract description 32
- IMQLKJBTEOYOSI-UHFFFAOYSA-N Phytic acid Natural products OP(O)(=O)OC1C(OP(O)(O)=O)C(OP(O)(O)=O)C(OP(O)(O)=O)C(OP(O)(O)=O)C1OP(O)(O)=O IMQLKJBTEOYOSI-UHFFFAOYSA-N 0.000 title claims abstract description 32
- 235000002949 phytic acid Nutrition 0.000 title claims abstract description 32
- 229940068041 phytic acid Drugs 0.000 title claims abstract description 32
- 239000000467 phytic acid Substances 0.000 title claims abstract description 32
- 238000002360 preparation method Methods 0.000 title claims abstract description 28
- YUWBVKYVJWNVLE-UHFFFAOYSA-N [N].[P] Chemical compound [N].[P] YUWBVKYVJWNVLE-UHFFFAOYSA-N 0.000 title claims description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims abstract description 52
- 238000000137 annealing Methods 0.000 claims abstract description 51
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- 238000006243 chemical reaction Methods 0.000 claims abstract description 28
- 239000003929 acidic solution Substances 0.000 claims abstract description 23
- ROOXNKNUYICQNP-UHFFFAOYSA-N ammonium persulfate Chemical compound [NH4+].[NH4+].[O-]S(=O)(=O)OOS([O-])(=O)=O ROOXNKNUYICQNP-UHFFFAOYSA-N 0.000 claims abstract description 22
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims abstract description 20
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 claims abstract description 19
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- 229910052698 phosphorus Inorganic materials 0.000 claims abstract description 19
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- 239000002243 precursor Substances 0.000 claims abstract description 18
- 229910052721 tungsten Inorganic materials 0.000 claims abstract description 17
- 239000000446 fuel Substances 0.000 claims abstract description 12
- 229910001870 ammonium persulfate Inorganic materials 0.000 claims abstract description 11
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 claims abstract description 11
- 239000010937 tungsten Substances 0.000 claims abstract description 11
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- 238000000034 method Methods 0.000 claims description 22
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 21
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- 229910021642 ultra pure water Inorganic materials 0.000 claims description 10
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- 230000007935 neutral effect Effects 0.000 claims description 6
- IYDGMDWEHDFVQI-UHFFFAOYSA-N phosphoric acid;trioxotungsten Chemical compound O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.OP(O)(O)=O IYDGMDWEHDFVQI-UHFFFAOYSA-N 0.000 claims description 5
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- LZKLAOYSENRNKR-LNTINUHCSA-N iron;(z)-4-oxoniumylidenepent-2-en-2-olate Chemical compound [Fe].C\C(O)=C\C(C)=O.C\C(O)=C\C(C)=O.C\C(O)=C\C(C)=O LZKLAOYSENRNKR-LNTINUHCSA-N 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 3
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- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 abstract description 39
- 239000003054 catalyst Substances 0.000 abstract description 28
- 230000003197 catalytic effect Effects 0.000 abstract description 12
- 229910052760 oxygen Inorganic materials 0.000 abstract description 12
- 239000001301 oxygen Substances 0.000 abstract description 12
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 11
- 230000009467 reduction Effects 0.000 abstract description 8
- 239000002253 acid Substances 0.000 abstract description 2
- 238000005406 washing Methods 0.000 abstract 1
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 21
- 238000012360 testing method Methods 0.000 description 16
- 238000006722 reduction reaction Methods 0.000 description 10
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 8
- 238000010438 heat treatment Methods 0.000 description 8
- WCUXLLCKKVVCTQ-UHFFFAOYSA-M Potassium chloride Chemical compound [Cl-].[K+] WCUXLLCKKVVCTQ-UHFFFAOYSA-M 0.000 description 7
- 230000000052 comparative effect Effects 0.000 description 6
- 239000007789 gas Substances 0.000 description 6
- 229910021389 graphene Inorganic materials 0.000 description 6
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- 229910052786 argon Inorganic materials 0.000 description 4
- 230000007423 decrease Effects 0.000 description 4
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- 238000000970 chrono-amperometry Methods 0.000 description 3
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- 239000005457 ice water Substances 0.000 description 3
- 239000011148 porous material Substances 0.000 description 3
- 239000010970 precious metal Substances 0.000 description 3
- CDVAIHNNWWJFJW-UHFFFAOYSA-N 3,5-diethoxycarbonyl-1,4-dihydrocollidine Chemical compound CCOC(=O)C1=C(C)NC(C)=C(C(=O)OCC)C1C CDVAIHNNWWJFJW-UHFFFAOYSA-N 0.000 description 2
- 238000002441 X-ray diffraction Methods 0.000 description 2
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- 239000010439 graphite Substances 0.000 description 2
- GXBKELQWVXYOPN-UHFFFAOYSA-N iron tungsten Chemical compound [W][Fe][W] GXBKELQWVXYOPN-UHFFFAOYSA-N 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
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- 229920006395 saturated elastomer Polymers 0.000 description 2
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 description 1
- 239000011865 Pt-based catalyst Substances 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
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- 229910052796 boron Inorganic materials 0.000 description 1
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- 238000003763 carbonization Methods 0.000 description 1
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- 238000001027 hydrothermal synthesis Methods 0.000 description 1
- 239000003999 initiator Substances 0.000 description 1
- 238000011031 large-scale manufacturing process Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 235000017807 phytochemicals Nutrition 0.000 description 1
- 229930000223 plant secondary metabolite Natural products 0.000 description 1
- 231100000572 poisoning Toxicity 0.000 description 1
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- 239000001103 potassium chloride Substances 0.000 description 1
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- 239000011593 sulfur Substances 0.000 description 1
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Abstract
Description
技术领域technical field
本发明属于燃料电池领域,具体涉及一种由植酸衍生的氮磷共掺杂的FeW/N,P-C复合材料及其制备与应用。The invention belongs to the field of fuel cells, in particular to a FeW/N,P-C composite material derived from phytic acid and co-doped with nitrogen and phosphorus, and its preparation and application.
背景技术Background technique
能源短缺和环境污染问题是21世纪以来人类社会发展所面临的两大难题。因此寻找洁净可再生能源及开发高效的能量储存和转换技术是当务之急。燃料电池作为一种最有可能得到大规模商业化应用的新能源技术得到了广泛关注,而氧气的电还原反应是最重要的电催化反应之一,广泛应用于燃料电池和金属-空气电池等领域。但燃料电池阴极氧还原反应需要催化剂,目前常用的催化剂为铂金或铂基催化剂,金属铂价格昂贵、储量有限、易中毒且长时间运行时性能损失严重等缺点限制了它的实际应用,也阻碍了燃料电池等相关领域的发展。Energy shortage and environmental pollution are two major problems faced by human society since the 21st century. Therefore, finding clean and renewable energy and developing efficient energy storage and conversion technologies are the top priorities. Fuel cells have attracted extensive attention as a new energy technology that is most likely to be commercialized on a large scale, and the electroreduction of oxygen is one of the most important electrocatalytic reactions, which are widely used in fuel cells and metal-air batteries. field. However, the oxygen reduction reaction of the fuel cell cathode requires a catalyst, and the commonly used catalysts are platinum or platinum-based catalysts. The disadvantages of platinum metal, such as high price, limited reserves, easy poisoning and serious performance loss during long-term operation, limit its practical application and hinder its practical application. The development of fuel cells and other related fields.
针对铂基催化剂的不足,近年来利用某些非金属元素(例如氮、硫、硼、磷)掺杂的碳材料表现出一定的氧还原性能,但元素掺杂涉及条件较苛刻,并且性能较之于商业化铂催化剂性能差较多,氧还原过电位较大。因此,现阶段的主要任务是开发低成本、高活性、高稳定性的阴极非贵金属催化剂,进而推动燃料电池的大规模商业化应用。In view of the deficiencies of platinum-based catalysts, carbon materials doped with some non-metallic elements (such as nitrogen, sulfur, boron, and phosphorus) have shown certain oxygen reduction performance in recent years, but element doping involves harsh conditions and has poor performance. Compared with commercial platinum catalysts, the performance is relatively poor, and the oxygen reduction overpotential is relatively large. Therefore, the main task at this stage is to develop low-cost, high-activity, and high-stability cathode non-precious metal catalysts, thereby promoting the large-scale commercial application of fuel cells.
此前,专利CN103920519B公开了一种基于铁钨双金属氧化物增强氮掺杂石墨烯的氧还原电催化剂的制备方法,包括以下步骤:1)将石墨粉进行氧化制备石墨氧化物;2)将步骤1)制备的石墨氧化物进行超声处理制备石墨烯氧化物;3)将步骤2)制备的石墨烯氧化物加水稀释并与氮源混合后水热反应,得到氮掺杂石墨烯;4)将步骤3)制备的氮掺杂石墨烯分散在水中后加入铁源和钨源,加热水解反应;5)将步骤4)的反应产物清洗干燥,然后在保护气的条件下热处理。虽然该专利公开了一种基于铁钨双金属氧化物增强氮掺杂石墨烯的氧还原电催化剂的制备方法,但该实验方法危险性较强,反应条件较为苛刻,本发明与之相比反应条件温和,安全系数高,操作性强,方法更为简单快捷。Previously, patent CN103920519B disclosed a preparation method of an oxygen reduction electrocatalyst based on iron-tungsten bimetallic oxides reinforced nitrogen-doped graphene, comprising the following steps: 1) oxidizing graphite powder to prepare graphite oxide; 2) oxidizing graphite powder; 1) the prepared graphite oxide is subjected to ultrasonic treatment to prepare graphene oxide; 3) the graphene oxide prepared in step 2) is diluted with water and mixed with a nitrogen source for hydrothermal reaction to obtain nitrogen-doped graphene; 4) the Step 3) The nitrogen-doped graphene prepared in step 3) is dispersed in water and then added with iron source and tungsten source, and heated for hydrolysis reaction; 5) The reaction product of step 4) is washed and dried, and then heat treated under the condition of protective gas. Although the patent discloses a preparation method of an oxygen reduction electrocatalyst based on iron-tungsten bimetallic oxides to enhance nitrogen-doped graphene, the experimental method is relatively dangerous and the reaction conditions are relatively harsh. The conditions are mild, the safety factor is high, the operability is strong, and the method is simpler and faster.
发明内容SUMMARY OF THE INVENTION
本发明的目的就是提供一种由植酸衍生的氮磷共掺杂的FeW/N,P-C复合材料及其制备与应用,解决了现有技术中Pt/C催化剂贵金属用量大、催化剂利用率低、催化活性低等技术问题,制得的复合材料具有良好的催化活性、稳定性以及甲醇耐受性,可用作燃料电池阴极氧还原催化剂,制备过程操作简单。The purpose of the present invention is to provide a nitrogen and phosphorus co-doped FeW/N, P-C composite material derived from phytic acid and its preparation and application, which solves the problem that the Pt/C catalyst has a large amount of precious metal and a low catalyst utilization rate in the prior art. , low catalytic activity and other technical problems, the prepared composite material has good catalytic activity, stability and methanol tolerance, can be used as a fuel cell cathode oxygen reduction catalyst, and the preparation process is simple to operate.
本发明的目的通过以下技术方案实现:The object of the present invention is achieved through the following technical solutions:
一种由植酸衍生的氮磷共掺杂的FeW/N,P-C复合材料的制备方法,所述制备方法具体包括以下步骤:A preparation method of a nitrogen-phosphorus co-doped FeW/N,P-C composite material derived from phytic acid, the preparation method specifically comprises the following steps:
(a)取含有苯胺、植酸和钨源的酸性溶液A和含有过硫酸铵和铁源的酸性溶液B,将酸性溶液B滴加至酸性溶液A中进行反应,经后处理得到FeW/N,P-C前驱体,该FeW/N,P-C前驱体呈墨绿色。其中苯胺可同时作为碳源与氮源,植酸可同时作为碳源与磷源,苯胺和植酸共同形成碳载体,过硫酸铵可作为引发剂诱导苯胺自聚合反应的发生;(a) take the acidic solution A containing aniline, phytic acid and tungsten source and the acidic solution B containing ammonium persulfate and iron source, add the acidic solution B dropwise to the acidic solution A to react, and obtain FeW/N through post-processing , P-C precursor, the FeW/N, P-C precursor is dark green. Among them, aniline can be used as carbon source and nitrogen source at the same time, phytic acid can be used as carbon source and phosphorus source at the same time, aniline and phytic acid together form a carbon carrier, and ammonium persulfate can be used as an initiator to induce the occurrence of aniline self-polymerization reaction;
(b)取步骤(a)所得的FeW/N,P-C前驱体与NaCl、KCl混合均匀,依次经过一次退火、酸洗和二次退火,得到FeW/N,P-C复合材料。(b) The FeW/N,P-C precursor obtained in step (a) is mixed uniformly with NaCl and KCl, and the FeW/N,P-C composite material is obtained by one annealing, pickling and second annealing in sequence.
步骤(a)中,所述酸性溶液A由浓度为0.5M的H2SO4溶液与超纯水按体积比1:(0.5-1)配制得到,体积为15-30mL,并含有苯胺、植酸和钨源;In step (a), the acidic solution A is prepared by H 2 SO 4 solution with a concentration of 0.5M and ultrapure water in a volume ratio of 1:(0.5-1), the volume is 15-30 mL, and contains aniline, phytochemicals acid and tungsten sources;
所述酸性溶液B由浓度为0.5M的H2SO4与超纯水按体积比1:(0.5-1)配制得到,并含有过硫酸铵和铁源。使用酸性溶液的目的是因为苯胺在酸性条件下聚合导电性较好。The acidic solution B is prepared from H 2 SO 4 with a concentration of 0.5M and ultrapure water in a volume ratio of 1:(0.5-1), and contains ammonium persulfate and iron source. The purpose of using an acidic solution is that aniline has better conductivity when polymerized under acidic conditions.
步骤(a)中,所述钨源采用磷钨酸,所述铁源采用乙酰丙酮铁,这两种有机化合物作为钨源与铁源更易于与苯胺和植酸发生反应。In step (a), phosphotungstic acid is used as the tungsten source, and iron acetylacetonate is used as the iron source, and these two organic compounds are more easily reacted with aniline and phytic acid as the tungsten source and the iron source.
步骤(a)中,苯胺、植酸、过硫酸铵和铁源的摩尔比为(1-2):(0.1-0.3):(0.5-1):(0.01-0.1),优选为1:0.125:0.75:0.05,铁源与钨源的摩尔比为(20-40):1,优选为20:1。In step (a), the molar ratio of aniline, phytic acid, ammonium persulfate and iron source is (1-2):(0.1-0.3):(0.5-1):(0.01-0.1), preferably 1:0.125 : 0.75: 0.05, and the molar ratio of the iron source to the tungsten source is (20-40): 1, preferably 20: 1.
步骤(a)中,反应的初始温度为0-5℃,优选为0℃,反应初期可采用冰水浴,低温反应1-4h(优选为2h)后,升温至室温继续反应20-24h,优选为22h,反应的同时进行搅拌。其中先低温诱导苯胺自聚合反应的发生,并控制初始反应速率,有效调节反应进程,随后升温至室温加速反应进行。In step (a), the initial temperature of the reaction is 0-5°C, preferably 0°C, an ice-water bath can be used in the initial stage of the reaction, and after the low-temperature reaction for 1-4h (preferably 2h), the temperature is raised to room temperature and the reaction is continued for 20-24h, preferably For 22h, the reaction was carried out while stirring. The aniline self-polymerization reaction is induced at a low temperature first, and the initial reaction rate is controlled to effectively adjust the reaction process, and then the temperature is raised to room temperature to accelerate the reaction.
步骤(a)中,所述后处理过程具体为:将反应完成的反应溶液进行抽滤,得到的滤渣水洗至中性,之后再用有机溶剂洗涤数次,然后进行真空干燥,干燥的温度为50-70℃,优选为60℃,干燥的时间为10-12h,优选为10h。In the step (a), the post-processing process is specifically as follows: the reaction solution after the reaction is subjected to suction filtration, the obtained filter residue is washed with water to neutrality, then washed with an organic solvent for several times, and then vacuum-dried, and the drying temperature is 50-70°C, preferably 60°C, and the drying time is 10-12h, preferably 10h.
步骤(b)中,FeW/N,P-C前驱体、NaCl和KCl的质量比为1:(5-20):(5-20),优选为1:10:10。作为模板化合物,NaCl、KCl在退火过程中随着温度的升高,逐渐熔化为液相态,使得复合材料各部分在高温下碳化反应完全。In step (b), the mass ratio of FeW/N, P-C precursor, NaCl and KCl is 1:(5-20):(5-20), preferably 1:10:10. As template compounds, NaCl and KCl gradually melt into liquid state with the increase of temperature during the annealing process, so that the carbonization reaction of each part of the composite material is complete at high temperature.
步骤(b)中,一次退火的温度为800-950℃,优选为850℃,一次退火的时间为1-4h,优选为2h,升温速率为1-5℃/min,优选为3℃/min,退火过程在惰性气氛In step (b), the temperature of one annealing is 800-950°C, preferably 850°C, the time of one annealing is 1-4h, preferably 2h, and the heating rate is 1-5°C/min, preferably 3°C/min , annealing process in an inert atmosphere
下进行,之后自然冷却至室温。惰性气氛可为氮气或氩气,作为保护气不与催化剂发生反应。若退火温度较低的话,材料的石墨化程度较差,材料导电性不好;若退火温度过高,材料会发生一定的坍塌与活性位点聚集,影响材料的整体性能,包括催化性能。and then cooled to room temperature naturally. The inert atmosphere can be nitrogen or argon, which does not react with the catalyst as a protective gas. If the annealing temperature is low, the degree of graphitization of the material is poor, and the conductivity of the material is not good; if the annealing temperature is too high, the material will collapse to a certain extent and the active sites will aggregate, which will affect the overall performance of the material, including catalytic performance.
步骤(b)中,酸洗过程具体为:将经一次退火后的中间产物分散于浓度为0.5M的H2SO4溶液中,在50-80℃(优选为60℃)下搅拌10-12h(优选为12h),之后抽滤得到滤渣,将滤渣水洗至中性,并用有机溶剂洗涤数次,再在50-70℃(优选为60℃)下真空干燥10-12h,优选为10h。酸洗可除去高温下聚集的纳米颗粒、团簇与过量NaCl、KCl化合物。In step (b), the pickling process is specifically as follows: dispersing the intermediate product after one annealing in a H 2 SO 4 solution with a concentration of 0.5M, and stirring at 50-80° C. (preferably 60° C.) for 10-12 h (preferably 12h), then suction filtration to obtain the filter residue, the filter residue is washed with water until neutral, and washed several times with an organic solvent, and then vacuum dried at 50-70°C (preferably 60°C) for 10-12h, preferably 10h. Pickling can remove nanoparticles, clusters and excess NaCl and KCl compounds aggregated at high temperature.
步骤(b)中,二次退火的温度为800-950℃,优选为850℃,二次退火的时间为1-4h,优选为2h,升温速率为1-5℃/min,优选为5℃/min,退火过程在惰性气氛下进行,之后自然冷却至室温。惰性气氛可为氮气或氩气,作为保护气不与复合材料发生反应,酸洗会破坏碳骨架的结构,二次退火处理稳定碳骨架。In step (b), the temperature of the secondary annealing is 800-950°C, preferably 850°C, the secondary annealing time is 1-4h, preferably 2h, and the heating rate is 1-5°C/min, preferably 5°C /min, the annealing process was carried out in an inert atmosphere, and then naturally cooled to room temperature. The inert atmosphere can be nitrogen or argon. As a protective gas, it does not react with the composite material. Pickling will destroy the structure of the carbon skeleton, and the secondary annealing treatment stabilizes the carbon skeleton.
一种如上述所述的制备方法制备得到的由植酸衍生的氮磷共掺杂的FeW/N,P-C复合材料,所述FeW/N,P-C复合材料呈多孔片层结构,孔容为0.693cm3/g,比表面积为737.93m2/g。FeW/N,P-C复合材料包含氮磷共掺杂的碳载体以及负载在碳载体上并以高度分散的原子形式存在的Fe和W。A FeW/N,PC composite material prepared by the above-mentioned preparation method and prepared by phytic acid-derived nitrogen and phosphorus co-doped, the FeW/N,PC composite material has a porous lamellar structure, and the pore volume is 0.693 cm 3 /g, the specific surface area was 737.93 m 2 /g. The FeW/N,PC composites contain nitrogen-phosphorus co-doped carbon supports and Fe and W supported on the carbon supports in the form of highly dispersed atoms.
一种如上述所述的由植酸衍生的氮磷共掺杂的FeW/N,P-C复合材料在燃料电池中的应用,该复合材料能高效地催化4e-氧还原反应,具有良好的催化活性、稳定性以及甲醇耐受性,可用作燃料电池阴极氧还原催化剂。A kind of FeW/N, P-C composite material with nitrogen and phosphorus co-doped from phytic acid as described above is used in fuel cell, the composite material can catalyze 4e-oxygen reduction reaction efficiently, and has good catalytic activity , stability and methanol tolerance, can be used as a fuel cell cathode oxygen reduction catalyst.
与现有技术相比,本发明具有以下有益效果:Compared with the prior art, the present invention has the following beneficial effects:
1、本发明通过精确控制配位环境和/或结构的孔容增加活性位点的密度,制备得到了氮磷掺杂的FeW/N,P-C片状复合材料,可以促进反应过程中O2和水的扩散、质子的传输以及电子在碳骨架中的传递等,进而提升催化性能。该复合材料具有较高催化活性、良好的稳定性与甲醇耐受性,表现出对ORR优异的催化活性,可用作燃料电池的阴极材料。1. The present invention increases the density of active sites by precisely controlling the coordination environment and/or the pore volume of the structure, and prepares a nitrogen-phosphorus-doped FeW/N, PC sheet-like composite material, which can promote O 2 and The diffusion of water, the transport of protons, and the transfer of electrons in the carbon skeleton can improve the catalytic performance. The composite material has high catalytic activity, good stability and methanol tolerance, exhibits excellent catalytic activity for ORR, and can be used as a cathode material for fuel cells.
2、与商用的Pt基催化剂相比,本发明的FeW/N,P-C复合材料在碱性介质中的ORR催化活性超过商业20%Pt/C催化剂,并且具有更高的稳定性和耐甲醇性能。2. Compared with commercial Pt-based catalysts, the ORR catalytic activity of the FeW/N,P-C composites of the present invention in alkaline medium exceeds that of commercial 20% Pt/C catalysts, and has higher stability and methanol resistance. .
3、本发明所采用的原料价格低廉且来源丰富,制备过程简单,有利于规模化生产,具有较高的实用价值。3. The raw materials used in the present invention are low in price, rich in sources, simple in preparation process, favorable for large-scale production, and have high practical value.
4、本发明的催化剂可克服传统的Pt/C催化剂贵金属用量大、催化剂利用效率低、催化活性低等技术问题。4. The catalyst of the present invention can overcome the technical problems of the traditional Pt/C catalyst, such as large amount of precious metal, low catalyst utilization efficiency and low catalytic activity.
附图说明Description of drawings
图1为实施例1制备得到的FeW/N,P-C复合材料的透射电镜图(TEM);Fig. 1 is the transmission electron microscope (TEM) of FeW/N, P-C composite material prepared in Example 1;
图2为实施例1制备得到的FeW/N,P-C复合材料的XRD图;Fig. 2 is the XRD pattern of FeW/N, P-C composite material prepared in Example 1;
图3为实施例1制备得到的FeW/N,P-C复合材料的XPS图;Fig. 3 is the XPS diagram of FeW/N, P-C composite material prepared in Example 1;
图4为实施例1和对比例1、对比例2的催化剂在0.1M KOH溶液中的线性极化曲线测试比较图;Fig. 4 is the linear polarization curve test comparison diagram of the catalysts of Example 1, Comparative Example 1 and Comparative Example 2 in 0.1M KOH solution;
图5为实施例1和对比例1的催化剂在0.1M KOH溶液中的计时电流比较图;Fig. 5 is a chronoamperometry comparison diagram of the catalysts of Example 1 and Comparative Example 1 in 0.1M KOH solution;
图6为实施例1和对比例1的催化剂在0.1M KOH溶液中的甲醇耐受性测试比较图。FIG. 6 is a comparison chart of the methanol tolerance test of the catalysts of Example 1 and Comparative Example 1 in 0.1M KOH solution.
具体实施方式Detailed ways
下面结合附图和具体实施例对本发明进行详细说明。The present invention will be described in detail below with reference to the accompanying drawings and specific embodiments.
实施例1Example 1
一种由植酸衍生的氮磷共掺杂的FeW/N,P-C复合材料,该复合材料呈多孔片状结构,采用以下步骤制备得到:A nitrogen and phosphorus co-doped FeW/N, P-C composite material derived from phytic acid, the composite material has a porous sheet-like structure, and is prepared by the following steps:
(1)制备FeW/N,P-C前驱体(1) Preparation of FeW/N, P-C precursors
将2mmol苯胺、0.25mmol植酸以及0.0025mmol磷钨酸均匀溶解分散于20mL的酸性溶液(由浓度为0.5M的H2SO4溶液与超纯水按体积比1:1)中,记为溶液A;将1.5mmol过硫酸铵、0.05mmol乙酰丙酮铁均匀溶解分散于酸性溶液(由浓度为0.5M的H2SO4溶液与超纯水按体积比1:1)中,记为溶液B。在冰水浴(0℃)的反应条件下,将溶液B缓慢滴加至溶液A中,反应2h后,升温至室温继续搅拌反应20h,之后将反应完成的反应溶液进行抽滤,得到的滤渣水洗至中性,之后再用有机溶剂洗涤数次,然后在60℃下真空干燥12h,得到墨绿色的FeW/N,P-C前驱体。2mmol of aniline, 0.25mmol of phytic acid and 0.0025mmol of phosphotungstic acid were uniformly dissolved and dispersed in 20mL of acidic solution (the H 2 SO 4 solution with a concentration of 0.5M and ultrapure water in a volume ratio of 1:1), denoted as solution A; 1.5mmol of ammonium persulfate and 0.05mmol of ferric acetylacetonate are uniformly dissolved and dispersed in an acidic solution (a 0.5M H 2 SO 4 solution and ultrapure water in a volume ratio of 1:1), which is designated as solution B. Under the reaction conditions of an ice-water bath (0°C), solution B was slowly added dropwise to solution A, and after 2 hours of reaction, the temperature was raised to room temperature and continued to stir for 20 hours. to neutrality, then washed with organic solvent for several times, and then vacuum-dried at 60 °C for 12 h to obtain dark green FeW/N, PC precursor.
(2)制备FeW/N,P-C复合材料(2) Preparation of FeW/N, P-C composites
按质量比1:10:10,取50mg的步骤(a)所得的FeW/N,P-C前驱体与500mg的NaCl、500mg的KCl混合均匀,依次经过一次退火、酸洗、二次退火等后处理过程,得到FeW/N,P-C复合材料,孔容为0.693cm3/g,比表面积为737.93m2/g。其中:一次退火的温度为850℃,一次退火的时间为2h,升温速率为3℃/min,退火过程在惰性气氛氮气作保护气下进行;酸洗过程具体为:将经一次退火后的中间产物分散于浓度为0.5M的H2SO4溶液中,在60℃下搅拌10h,之后抽滤得到滤渣,将滤渣水洗至中性,并用有机溶剂洗涤数次,再在60℃下真空干燥12h;二次退火的温度为850℃,退火时间为2h,二次退火的升温速率为5℃/min,退火过程在惰性气氛氮气下进行。According to the mass ratio of 1:10:10, take 50 mg of FeW/N obtained in step (a), and mix the PC precursor with 500 mg of NaCl and 500 mg of KCl, and then undergo post-treatment such as primary annealing, pickling, and secondary annealing in turn. During the process, FeW/N, PC composite material was obtained with a pore volume of 0.693 cm 3 /g and a specific surface area of 737.93 m 2 /g. Among them: the temperature of one annealing is 850℃, the time of one annealing is 2h, the heating rate is 3℃/min, and the annealing process is carried out under inert atmosphere nitrogen as protective gas; The product was dispersed in H 2 SO 4 solution with a concentration of 0.5M, stirred at 60°C for 10h, and then suction filtered to obtain a filter residue. The filter residue was washed with water until neutral, washed with organic solvent for several times, and then vacuum-dried at 60°C for 12h ; The temperature of the secondary annealing is 850°C, the annealing time is 2h, the heating rate of the secondary annealing is 5°C/min, and the annealing process is carried out in an inert atmosphere of nitrogen.
该FeW/N,P-C复合材料的透射电镜图(TEM)如图1所示(左图为200nm,),可看到,制备的FeW/N,P-C复合材料具有明显的片状结构,且没有观察到Fe、W纳米颗粒的存在,表明Fe、W两种元素可能没有形成团簇或颗粒,可能是以高度分散的原子形式存在,右图中的小图则表明该复合材料为多晶态物质,这也说明本发明合成方法的可靠性。The transmission electron microscope (TEM) image of the FeW/N,P-C composite material is shown in Figure 1 (the left picture is 200 nm), it can be seen that the prepared FeW/N,P-C composite material has obvious sheet-like structure, and no The existence of Fe and W nanoparticles was observed, indicating that the two elements Fe and W may not form clusters or particles, but may exist in the form of highly dispersed atoms. The small image on the right shows that the composite material is polycrystalline material, which also shows the reliability of the synthesis method of the present invention.
该FeW/N,P-C复合材料的XRD图如图3所示,可看到,该复合材料中没有形成Fe、W等晶体颗粒,只有石墨化碳的峰,表明Fe、W可能以掺杂的形式存在于催化剂中,结合图2、3说明制得的材料确实是FeW/N,P-C。The XRD pattern of the FeW/N,P-C composite material is shown in Figure 3. It can be seen that no crystal particles such as Fe and W are formed in the composite material, but only the peaks of graphitized carbon, indicating that Fe and W may be doped with The form exists in the catalyst, and the material obtained is indeed FeW/N, P-C with reference to Figures 2 and 3.
将该FeW/N,P-C复合材料作为氧还原催化剂进行线性极化测试,测试条件为:采用浓度为0.1M的KOH溶液,测试参数为-0.8~0.2V,扫速为5mV/s,转速为1600rpm(下同),结果如图4所示,可看到,FeW/N,P-C复合材料的起始电位表现为0.995V(vs.RHE),半波电位为0.877V(vs.RHE),在0.85V时的极限电流密度为-3.36mA cm-2。The FeW/N, PC composite was used as an oxygen reduction catalyst for linear polarization test. The test conditions were as follows: KOH solution with a concentration of 0.1M was used. 1600rpm (the same below), the results are shown in Figure 4, it can be seen that the initial potential of FeW/N, PC composite material is 0.995V (vs.RHE), the half-wave potential is 0.877V (vs.RHE), The limiting current density at 0.85V is -3.36mA cm -2 .
将该FeW/N,P-C复合材料进行计时电流测试,测试条件为:采用O2饱和的浓度为0.1M KOH的溶液中,测试参数为-0.15V,转速为1600rpm,测试时间为50000s(下同),结果如图5所示,可看到,随着测试时间的推移,FeW/N,P-C复合材料的稳定性逐渐降低,但下降的速率非常缓慢,在50000s测试之后,FeW/N,P-C复合材料可以保持初始电流密度的93.92%。The FeW/N, PC composite material was tested by chronoamperometry, and the test conditions were as follows: in a solution with a concentration of 0.1M KOH saturated with O2 , the test parameters were -0.15V, the rotating speed was 1600rpm, and the test time was 50000s (the same below). ), the results are shown in Figure 5. It can be seen that the stability of FeW/N, PC composites gradually decreases with the passage of test time, but the rate of decline is very slow. After 50000s test, FeW/N, PC The composite material can maintain 93.92% of the initial current density.
将该FeW/N,P-C复合材料进行抗甲醇测试,测试条件为:采用O2饱和的浓度为0.1M的KOH溶液,测试参数为-0.15V,转速为1600rpm,测试时间为5000s。在测试开始1000s时,向KOH溶液中快速加入3M的甲醇(下同),结果如图6所示,可看到,加入甲醇之后,FeW/N,P-C复合材料的电流仅有小幅度的变化。The FeW/N, PC composites were tested for methanol resistance. The test conditions were as follows: KOH solution with a concentration of 0.1M saturated with O 2 was used, the test parameters were -0.15V, the rotation speed was 1600rpm, and the test time was 5000s. At the beginning of the test for 1000s, 3M methanol (the same below) was rapidly added to the KOH solution. The results are shown in Figure 6. It can be seen that after the addition of methanol, the current of FeW/N, PC composites only changed slightly .
对比例1Comparative Example 1
一种商业催化剂JM 20%Pt/C,购自Johnson-Matthery,对其进行在碱性溶液中的线性极化曲线测试,结果具体如图4所示,可看到,JM 20%Pt/C的起始电位:0.990V;半波电位:0.861V;在0.85V时极限电流密度:-3.01mAcm-2。对该商业催化剂进行计时电流测试,结果如图5所示,可看到随着测试时间的推移,JM20%Pt/C的稳定性逐渐降低,但下降的速率非常快,在50000s测试之后,商业JM20%Pt/C的电流密度仅保持在初始电流密度的44.57%。对该商业催化剂进行抗甲醇测试,结果如图6所示,可看到,加入甲醇之后,JM20%Pt/C催化剂的电流则发生一个明显的变化,即JM 20%Pt/C催化剂在含有甲醇的碱性溶液中发生了剧烈的氧化反应。A
图4可说明制备的FeW/N,P-C复合材料对氧还原反应有较高的催化活性,足以和商业化的催化剂相媲美。Figure 4 shows that the prepared FeW/N,P-C composites have high catalytic activity for the oxygen reduction reaction, which is comparable to that of commercial catalysts.
图5中可看出FeW/N,P-C复合材料的电流衰减速率明显慢于商业JM 20%Pt/C,说明FeW/N,P-C复合材料在上述条件下的稳定性远优于商业JM 20%Pt/C。It can be seen in Fig. 5 that the current decay rate of FeW/N,P-C composite is significantly slower than that of
图6说明FeW/N,P-C复合材料的甲醇耐受性优于JM 20%Pt/C催化剂。Figure 6 illustrates that the methanol tolerance of FeW/N,P-C composite is better than that of
综上所述,本发明提供了一种由植酸衍生的氮磷共掺杂的FeW/N,P-C复合材料的制备方法,制备得到的复合材料为均匀的多孔片状结构,并且在氧还原过程中表现出显著增强的电化学性能。To sum up, the present invention provides a method for preparing a FeW/N,P-C composite material derived from phytic acid, which is co-doped with nitrogen and phosphorus. The process exhibits significantly enhanced electrochemical performance.
对比例2Comparative Example 2
一种氮掺杂的FeW/N-C复合材料,该复合材料在制备过程中除不添加植酸外,均采用与实施例1相同的步骤制备。对其进行在碱性溶液中的线性极化曲线测试,结果具体如图4所示,可看到,FeW/N-C复合材料的起始电位:0.893V;半波电位:0.799V;在0.85V时极限电流密度:-0.50mAcm-2。图4可说明制备的FeW/N,P-C复合材料比FeW/N-C复合材料有更高的催化活性。A nitrogen-doped FeW/NC composite material was prepared by the same steps as in Example 1 except that phytic acid was not added during the preparation process. The linear polarization curve test in alkaline solution was carried out. The results are shown in Figure 4. It can be seen that the initial potential of FeW/NC composite material: 0.893V; half-wave potential: 0.799V; at 0.85V Time limiting current density: -0.50mAcm -2 . Figure 4 can illustrate that the prepared FeW/N, PC composites have higher catalytic activity than FeW/NC composites.
实施例2Example 2
一种由植酸衍生的氮磷共掺杂的FeW/N,P-C复合材料,该复合材料呈多孔片状结构,采用以下步骤制备得到:A nitrogen and phosphorus co-doped FeW/N, P-C composite material derived from phytic acid, the composite material has a porous sheet-like structure, and is prepared by the following steps:
(1)制备FeW/N,P-C前驱体(1) Preparation of FeW/N, P-C precursors
将1mmol苯胺、0.1mmol植酸以及0.0005mmol磷钨酸均匀溶解分散于20mL的酸性溶液(由浓度为0.5M的H2SO4溶液与超纯水按体积比1:0.5)中,记为溶液A;将0.5mmol过硫酸铵、0.01mmol乙酰丙酮铁均匀溶解分散于酸性溶液(由浓度为0.5M的H2SO4溶液与超纯水按体积比1:0.5)中,记为溶液B。在5℃的反应条件下,将溶液B缓慢滴加至溶液A中,反应1h后,升温至室温继续搅拌反应20h,之后将反应完成的反应溶液进行抽滤,得到的滤渣水洗至中性,之后再用有机溶剂洗涤数次,然后在50℃下真空干燥12h,得到墨绿色的FeW/N,P-C前驱体。1mmol of aniline, 0.1mmol of phytic acid and 0.0005mmol of phosphotungstic acid were uniformly dissolved and dispersed in 20mL of acidic solution (the H 2 SO 4 solution with a concentration of 0.5M and ultrapure water in a volume ratio of 1:0.5), denoted as solution A; 0.5 mmol ammonium persulfate and 0.01 mmol iron acetylacetonate are uniformly dissolved and dispersed in an acidic solution (from H 2 SO 4 solution with a concentration of 0.5 M to ultrapure water in a volume ratio of 1:0.5), which is designated as solution B. Under the reaction conditions of 5 °C, solution B was slowly added dropwise to solution A. After reacting for 1 hour, the temperature was raised to room temperature and the reaction was continued for 20 hours. After that, it was washed several times with an organic solvent, and then vacuum-dried at 50 °C for 12 h to obtain a dark green FeW/N, PC precursor.
(2)制备FeW/N,P-C复合材料(2) Preparation of FeW/N, P-C composites
按质量比1:5:5,取50mg的步骤(a)所得的FeW/N,P-C前驱体与250mg的NaCl、250mg的KCl混合均匀,依次经过一次退火、酸洗、二次退火等后处理过程,得到FeW/N,P-C复合材料。其中:一次退火的温度为800℃,一次退火的时间为4h,升温速率为3℃/min,退火过程在惰性气氛氮气作保护气下进行;酸洗过程具体为:将经一次退火后的中间产物分散于浓度为0.5M的H2SO4溶液中,在80℃下搅拌10h,之后抽滤得到滤渣,将滤渣水洗至中性,并用有机溶剂洗涤数次,再在70℃下真空干燥10h;二次退火的温度为800℃,退火时间为4h,二次退火的升温速率为5℃/min,退火过程在惰性气氛氮气下进行。According to the mass ratio of 1:5:5, take 50 mg of FeW/N obtained in step (a), and mix the PC precursor with 250 mg of NaCl and 250 mg of KCl, and then undergo post-processing such as primary annealing, pickling, and secondary annealing in turn. process to obtain FeW/N, PC composites. Among them: the temperature of one annealing is 800℃, the time of one annealing is 4h, the heating rate is 3℃/min, and the annealing process is carried out under inert atmosphere nitrogen as protective gas; The product was dispersed in H 2 SO 4 solution with a concentration of 0.5M, stirred at 80°C for 10h, and then suction filtered to obtain a filter residue. The filter residue was washed with water until neutral, washed with organic solvent for several times, and then vacuum-dried at 70°C for 10h ; The temperature of the secondary annealing is 800°C, the annealing time is 4h, the heating rate of the secondary annealing is 5°C/min, and the annealing process is carried out in an inert atmosphere nitrogen.
实施例3Example 3
一种由植酸衍生的氮磷共掺杂的FeW/N,P-C复合材料,该复合材料呈多孔片状结构,采用以下步骤制备得到:A nitrogen and phosphorus co-doped FeW/N, P-C composite material derived from phytic acid, the composite material has a porous sheet-like structure, and is prepared by the following steps:
(1)制备FeW/N,P-C前驱体(1) Preparation of FeW/N, P-C precursors
将2mmol苯胺、0.3mmol植酸以及0.0025mmol磷钨酸均匀溶解分散于20mL的酸性溶液(由浓度为0.5M的H2SO4溶液与超纯水按体积比1:0.75)中,记为溶液A;将1mmol过硫酸铵、0.1mmol乙酰丙酮铁均匀溶解分散于酸性溶液(由浓度为0.5M的H2SO4溶液与超纯水按体积比1:0.75)中,记为溶液B。在冰水浴(0℃)的反应条件下,将溶液B缓慢滴加至溶液A中,反应4h后,升温至室温继续搅拌反应24h,之后将反应完成的反应溶液进行抽滤,得到的滤渣水洗至中性,之后再用有机溶剂洗涤数次,然后在70℃下真空干燥10h,得到墨绿色的FeW/N,P-C前驱体。2mmol of aniline, 0.3mmol of phytic acid and 0.0025mmol of phosphotungstic acid were uniformly dissolved and dispersed in 20mL of acidic solution (the H 2 SO 4 solution with a concentration of 0.5M and ultrapure water in a volume ratio of 1:0.75), denoted as solution A; 1 mmol ammonium persulfate and 0.1 mmol ferric acetylacetonate are uniformly dissolved and dispersed in an acidic solution (a 0.5 M H 2 SO 4 solution and ultrapure water in a volume ratio of 1:0.75), which is designated as solution B. Under the reaction conditions of an ice-water bath (0°C), solution B was slowly added dropwise to solution A, and after 4 hours of reaction, the temperature was raised to room temperature and the reaction was continued for 24 hours. to neutrality, then washed with organic solvent for several times, and then vacuum-dried at 70 °C for 10 h to obtain a dark green FeW/N, PC precursor.
(2)制备FeW/N,P-C复合材料(2) Preparation of FeW/N, P-C composites
按质量比1:20:20,取50mg的步骤(a)所得的FeW/N,P-C前驱体与1000mg的NaCl、1000mg的KCl混合均匀,依次经过一次退火、酸洗、二次退火等后处理过程,得到FeW/N,P-C复合材料。其中:一次退火的温度为950℃,一次退火的时间为1h,升温速率为3℃/min,退火过程在惰性气氛氩气作保护气下进行;酸洗过程具体为:将经一次退火后的中间产物分散于浓度为0.5M的H2SO4溶液中,在50℃下搅拌12h,之后抽滤得到滤渣,将滤渣水洗至中性,并用有机溶剂洗涤数次,再在50℃下真空干燥10h;二次退火的温度为950℃,退火时间为1h,二次退火的升温速率为5℃/min,退火过程在惰性气氛氩气下进行。According to the mass ratio of 1:20:20, take 50 mg of FeW/N obtained in step (a), the PC precursor is mixed with 1000 mg of NaCl and 1000 mg of KCl, and then undergoes a post-treatment such as annealing, pickling, and secondary annealing. process to obtain FeW/N, PC composites. Among them: the temperature of one annealing is 950℃, the time of one annealing is 1h, the heating rate is 3℃/min, and the annealing process is carried out in an inert atmosphere with argon as protective gas; The intermediate product was dispersed in H 2 SO 4 solution with a concentration of 0.5M, stirred at 50 °C for 12 h, and then suction filtered to obtain a filter residue. The filter residue was washed with water until neutral, washed with organic solvent for several times, and then vacuum-dried at 50 °C 10h; the temperature of the secondary annealing is 950°C, the annealing time is 1h, the heating rate of the secondary annealing is 5°C/min, and the annealing process is carried out in an inert atmosphere of argon.
上述的对实施例的描述是为便于该技术领域的普通技术人员能理解和使用发明。熟悉本领域技术的人员显然可以容易地对这些实施例做出各种修改,并把在此说明的一般原理应用到其他实施例中而不必经过创造性的劳动。因此,本发明不限于上述实施例,本领域技术人员根据本发明的揭示,不脱离本发明范畴所做出的改进和修改都应该在本发明的保护范围之内。The foregoing description of the embodiments is provided to facilitate understanding and use of the invention by those of ordinary skill in the art. It will be apparent to those skilled in the art that various modifications to these embodiments can be readily made, and the generic principles described herein can be applied to other embodiments without inventive step. Therefore, the present invention is not limited to the above-mentioned embodiments, and improvements and modifications made by those skilled in the art according to the disclosure of the present invention without departing from the scope of the present invention should all fall within the protection scope of the present invention.
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