CN106910899B - A kind of preparation method of nitrogen-doped double-shell structure nanocatalyst - Google Patents

A kind of preparation method of nitrogen-doped double-shell structure nanocatalyst Download PDF

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CN106910899B
CN106910899B CN201710108662.4A CN201710108662A CN106910899B CN 106910899 B CN106910899 B CN 106910899B CN 201710108662 A CN201710108662 A CN 201710108662A CN 106910899 B CN106910899 B CN 106910899B
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palladium
cobalt
platinum
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尹诗斌
陆家佳
张力上
罗林
沈培康
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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
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    • BPERFORMING OPERATIONS; TRANSPORTING
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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
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    • H01M4/86Inert electrodes with catalytic activity, e.g. for fuel cells
    • H01M4/90Selection of catalytic material
    • H01M4/92Metals of platinum group
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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
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    • H01M4/86Inert electrodes with catalytic activity, e.g. for fuel cells
    • H01M4/90Selection of catalytic material
    • H01M4/92Metals of platinum group
    • H01M4/925Metals of platinum group supported on carriers, e.g. powder carriers
    • H01M4/926Metals of platinum group supported on carriers, e.g. powder carriers on carbon or graphite
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Abstract

The invention discloses a preparation method of a nitrogen-doped double-shell structure nano catalyst, which comprises the following operation steps: (1) adding a carrier and a metal precursor into a solvent, stirring, adding a reducing agent for reduction, filtering, cleaning and drying to obtain a primary product; (2) placing the mixture in a high-temperature reaction furnace, introducing gas and calcining to obtain a nitrogen-doped nano alloy catalyst; (3) and performing dealloying treatment to obtain the nitrogen-doped double-shell structure nano catalyst. The catalyst has 5-19 times of activity of commercial 20 wt% Pt/C catalyst in oxygen reduction mass at 0.9V, has higher oxygen reduction catalytic performance, and lays a technical foundation for large-scale application of proton exchange membrane fuel cells.

Description

一种氮掺杂双壳层结构纳米催化剂的制备方法A kind of preparation method of nitrogen-doped double-shell structure nanocatalyst

技术领域technical field

本发明涉及一种纳米催化剂的制备方法,特别涉及一种氮掺杂双壳层结构纳米催化剂的制备方法。The invention relates to a preparation method of a nano-catalyst, in particular to a preparation method of a nitrogen-doped double-shell structure nano-catalyst.

背景技术Background technique

目前,随着能源需求的不断增长和环保意识的不断增强,急需开发清洁的能源转换技术。质子交换膜燃料电池提供了一种有希望的清洁能源转换途径,但是其商业化存在成本高和稳定性差等问题。铂是质子交换膜燃料电池高效的催化剂,但是,由于其在地壳中的含量极低,且在汽车工业中的需求日益增长,所以研究者致力于开发高效的非贵金属催化剂和低含量贵金属催化剂。At present, with the continuous growth of energy demand and the continuous enhancement of environmental protection awareness, the development of clean energy conversion technology is urgently needed. Proton exchange membrane fuel cells offer a promising pathway for clean energy conversion, but their commercialization suffers from high cost and poor stability. Platinum is an efficient catalyst for proton exchange membrane fuel cells. However, due to its extremely low content in the earth's crust and its growing demand in the automotive industry, researchers are working to develop high-efficiency non-precious metal catalysts and low-content precious metal catalysts.

公开于该背景技术部分的信息仅仅旨在增加对本发明的总体背景的理解,而不应当被视为承认或以任何形式暗示该信息构成已为本领域一般技术人员所公知的现有技术。The information disclosed in this Background section is only for enhancement of understanding of the general background of the invention and should not be taken as an acknowledgement or any form of suggestion that this information forms the prior art already known to a person of ordinary skill in the art.

发明内容SUMMARY OF THE INVENTION

本发明针对现有技术的不足,发明一种氮掺杂双壳层结构纳米催化剂的制备方法,旨在得到一种工艺简洁、成本低、催化性能好的氮掺杂双壳层结构纳米催化剂。Aiming at the deficiencies of the prior art, the present invention invents a method for preparing a nitrogen-doped double-shell structure nanocatalyst, aiming to obtain a nitrogen-doped double-shell structure nanocatalyst with simple process, low cost and good catalytic performance.

为实现上述目的,本发明提供的技术方案如下:For achieving the above object, the technical scheme provided by the invention is as follows:

一种氮掺杂双壳层结构纳米催化剂的制备方法,包含以下操作步骤:A method for preparing a nitrogen-doped double-shell structure nanocatalyst, comprising the following operation steps:

(1)催化剂的还原:将载体和金属前驱体加入溶剂中,然后超声搅拌,再加入还原剂,加热还原,将还原所得混合物过滤、清洗、干燥,得到初级产品;(1) reduction of the catalyst: add the carrier and the metal precursor into the solvent, then ultrasonically stir, add a reducing agent, heat and reduce, filter, wash and dry the mixture obtained from the reduction to obtain a primary product;

(2)催化剂的高温煅烧:将步骤(1)所得初级产品置于高温反应炉中,高温反应炉可程序控温,并通入气体进行高温煅烧,即得氮掺杂的纳米合金催化剂;(2) high-temperature calcination of catalyst: the primary product obtained in step (1) is placed in a high-temperature reaction furnace, and the temperature of the high-temperature reaction furnace can be controlled by a program, and gas is introduced for high-temperature calcination to obtain a nitrogen-doped nano-alloy catalyst;

(3)去合金化处理:将步骤(2)所得氮掺杂的纳米合金催化剂进行去合金化处理,得到氮掺杂双壳层结构的纳米催化剂。(3) dealloying treatment: the nitrogen-doped nano-alloy catalyst obtained in step (2) is subjected to deal-alloying treatment to obtain a nano-catalyst with a nitrogen-doped double-shell structure.

其中,步骤(1)中所述的载体为碳黑、碳纳米管、碳纤维、碳纳米棒、石墨烯、氧化石墨烯、还原氧化石墨烯、活性炭、多孔碳中的任意一种或几种的组合;所述的溶剂为去离子水、乙醇、异丙醇、乙二醇中的任意一种或几种的组合。Wherein, the carrier described in the step (1) is any one or more of carbon black, carbon nanotubes, carbon fibers, carbon nanorods, graphene, graphene oxide, reduced graphene oxide, activated carbon, and porous carbon. combination; the solvent is any one or a combination of deionized water, ethanol, isopropanol, and ethylene glycol.

其中,步骤(1)中所述的金属前驱体为由Ⅰ类和Ⅱ类金属前驱体组成,所述的Ⅰ类为铂盐和/或钯盐,Ⅱ类为铁盐、钴盐、镍盐、钨盐、钼盐或钒盐中的一种或两种混合。Wherein, the metal precursors described in step (1) are composed of class I and class II metal precursors, the class I is platinum salt and/or palladium salt, and class II is iron salt, cobalt salt, nickel salt , tungsten salt, molybdenum salt or vanadium salt in one or two mixtures.

其中,所述金属前驱体组合方式有:铂铁钨,铂铁钼,铂铁钒,铂钴钨,铂钴钼,铂钴钒,铂镍钨,铂镍钼,铂镍钒,钯铁钨,钯铁钼,钯铁钒,钯钴钨,钯钴钼,钯钴钒,钯镍钨,钯镍钼,钯镍钒,铂铁钴,铂铁镍,铂钴镍,铂钨钼,铂钨钒,铂钼钒,钯铁钴,钯铁镍,钯钴镍,钯钨钼,钯钨钒,钯钼钒,铂钯铁,铂钯钴,铂钯镍,铂钯钨,铂钯钼,铂钯钒;组合中的三种元素之间的摩尔比1~10:1~20:1~20。Wherein, the combinations of the metal precursors include: platinum iron tungsten, platinum iron molybdenum, platinum iron vanadium, platinum cobalt tungsten, platinum cobalt molybdenum, platinum cobalt vanadium, platinum nickel tungsten, platinum nickel molybdenum, platinum nickel vanadium, palladium iron tungsten , palladium iron molybdenum, palladium iron vanadium, palladium cobalt tungsten, palladium cobalt molybdenum, palladium cobalt vanadium, palladium nickel tungsten, palladium nickel molybdenum, palladium nickel vanadium, platinum iron cobalt, platinum iron nickel, platinum cobalt nickel, platinum tungsten molybdenum, platinum Tungsten vanadium, platinum molybdenum vanadium, palladium iron cobalt, palladium iron nickel, palladium cobalt nickel, palladium tungsten molybdenum, palladium tungsten vanadium, palladium molybdenum vanadium, platinum palladium iron, platinum palladium cobalt, platinum palladium nickel, platinum palladium tungsten, platinum palladium molybdenum , platinum palladium vanadium; the molar ratio between the three elements in the combination is 1-10:1-20:1-20.

其中,所述的铂盐为氯铂酸、乙酰丙酮铂、六氯铂酸铵、六氯铂酸钾、六氯铂酸钠、四氯铂酸钾、氯亚铂酸钠、四氯化铂、硝酸铂、四氨合硝酸铂、氯化四氨合铂;所述的钯盐为氯化钯、乙酸钯、氯亚钯酸铵、氯钯酸钾、硫酸钯、硝酸亚钯、四氯钯酸钠、四氯钯酸钾、四溴钯酸钾、二溴化钯、三氟乙酸钯、乙酰丙酮钯、二氯二氨钯、四氨基硝酸钯、六氟乙酰丙酮钯、三苯基膦醋酸钯、四(三苯基膦)钯、双(苄腈)二氯化钯、二(三苯基膦)氯化钯、三(苄亚基丙酮)二钯、双(二亚苄基丙酮)钯、三(二亚苄基丙酮)二钯、(1,5-环辛二烯)二氯化钯、(1,3-双(二苯基膦)丙烷)氯化钯、1,2-二(二苯基膦基)乙烷二氯化钯;所述的铁盐为三氯化铁、氯化亚铁、乙酰丙酮铁、铁氰化钾、亚铁氰化钠、亚硝基亚铁氰化钠、二茂铁、硝酸铁、柠檬酸铁、柠檬酸铁铵、草酸高铁铵、草酸亚铁、六氰合铁酸钾、硫酸铁、硫酸亚铁、硫酸亚铁铵、硫酸高铁铵;所述的钴盐为氯化钴、乙酸钴、磷酸钴、酞菁钴、钴氰化钾、六氰钴酸钾、六氨基氯化钴、高氯酸钴、硝酸钴、氟化钴、碘化钴、溴化钴、亚硝酸钴钠、草酸钴、硫酸钴、硫酸亚钴、硫酸钴铵、环烷酸钴、乙酰丙酮钴;所述的镍盐为氯化镍、乙酰丙酮镍、乙酰丙酮酸镍、乙酸镍、溴化镍、碘化镍、硫酸镍、硝酸镍、硫酸镍铵、次磷酸镍、硝酸镍铵、氨基磺酸镍、碱式碳酸镍、甲酸镍、二茂镍、二(三苯基膦)溴化镍、双(三苯基膦)氯化镍;所述的钨盐为偏钨酸铵、钨酸铵、钨酸钾、钨酸钠、磷钨酸、磷钨酸钠、钨硅酸、六氯化钨、六羰基钨、异丙醇钨;所述的钼盐为钼酸、四钼酸铵、七钼酸铵、二钼酸铵、钼酸钠、磷钼酸、磷钼酸铵、磷钼酸钠、氯化钼、钼酸锂、钼酸钾、六羰基钼、乙酰丙酮钼、异丙醇钼;所述的钒盐为偏钒酸铵、偏钒酸钠、偏钒酸钾、正钒酸钠、氯化钒、氧化钒、四氯化钒、钒酸钠、乙酰丙酮钒、三异丙醇氧钒、乙酰丙酮氧钒、三异丙氧基氧化钒、氧化二乙酰丙酮合钒。Wherein, the platinum salt is chloroplatinic acid, platinum acetylacetonate, ammonium hexachloroplatinate, potassium hexachloroplatinate, sodium hexachloroplatinate, potassium tetrachloroplatinate, sodium chloroplatinite, platinum tetrachloride , platinum nitrate, tetraammine platinum nitrate, tetraammine platinum chloride; Described palladium salt is palladium chloride, palladium acetate, ammonium chloropalladite, potassium chloropalladate, palladium sulfate, palladium nitrate, tetrachloride Sodium palladate, potassium tetrachloropalladate, potassium tetrabromopalladate, palladium dibromide, palladium trifluoroacetate, palladium acetylacetonate, palladium dichlorodiamine, palladium tetraamino nitrate, palladium hexafluoroacetylacetonate, triphenyl Phosphine palladium acetate, tetrakis(triphenylphosphine) palladium, bis(benzonitrile) palladium dichloride, bis(triphenylphosphine) palladium chloride, tris(benzylideneacetone)dipalladium, bis(dibenzylidene) Acetone) palladium, tris(dibenzylideneacetone)dipalladium, (1,5-cyclooctadiene)palladium dichloride, (1,3-bis(diphenylphosphine)propane)palladium chloride, 1, 2-bis(diphenylphosphino)ethane palladium dichloride; Described iron salt is ferric chloride, ferrous chloride, ferric acetylacetonate, potassium ferricyanide, sodium ferrocyanide, nitrous Sodium ferrocyanide, ferrocene, ferric nitrate, ferric citrate, ferric ammonium citrate, ferric ammonium oxalate, ferrous oxalate, potassium hexacyanoferrate, ferric sulfate, ferrous sulfate, ferrous ammonium sulfate, Ferric ammonium sulfate; the cobalt salts are cobalt chloride, cobalt acetate, cobalt phosphate, cobalt phthalocyanine, potassium cobalt cyanide, potassium hexacyanocobaltate, hexaamino cobalt chloride, cobalt perchlorate, cobalt nitrate, fluorine Cobalt oxide, cobalt iodide, cobalt bromide, sodium cobalt nitrite, cobalt oxalate, cobalt sulfate, cobaltous sulfate, cobalt ammonium sulfate, cobalt naphthenate, cobalt acetylacetonate; Nickel acetone, nickel acetylacetonate, nickel acetate, nickel bromide, nickel iodide, nickel sulfate, nickel nitrate, nickel ammonium sulfate, nickel hypophosphite, nickel ammonium nitrate, nickel sulfamate, basic nickel carbonate, nickel formate, Nickellocene, bis(triphenylphosphine) nickel bromide, bis(triphenylphosphine) nickel chloride; the tungsten salts are ammonium metatungstate, ammonium tungstate, potassium tungstate, sodium tungstate, phosphorus Tungstic acid, sodium phosphotungstate, tungstosilicic acid, tungsten hexachloride, tungsten hexacarbonyl, tungsten isopropoxide; the molybdenum salts are molybdic acid, ammonium tetramolybdate, ammonium heptamolybdate, ammonium dimolybdate, Sodium molybdate, phosphomolybdic acid, ammonium phosphomolybdate, sodium phosphomolybdate, molybdenum chloride, lithium molybdate, potassium molybdate, molybdenum hexacarbonyl, molybdenum acetylacetonate, molybdenum isopropoxide; described vanadium salt is partial Ammonium vanadate, sodium metavanadate, potassium metavanadate, sodium orthovanadate, vanadium chloride, vanadium oxide, vanadium tetrachloride, sodium vanadate, vanadium acetylacetonate, vanadyl triisopropoxide, vanadyl acetylacetonate , triisopropoxy vanadium oxide, vanadium oxide diacetylacetonate.

其中,步骤(1)中所述的载体与金属前驱体中含有的金属的质量比是0.25~99:1。Wherein, the mass ratio of the carrier described in step (1) to the metal contained in the metal precursor is 0.25-99:1.

其中,步骤(1)中所述的加热还原的温度是40~200摄氏度,还原时间0.1~100小时;所述的加热的方式为水浴加热、油浴加热、沙浴加热或高温反应釜中的任意一种。Wherein, the temperature of the heating reduction described in the step (1) is 40~200 degrees Celsius, and the reduction time is 0.1~100 hours; the heating mode is water bath heating, oil bath heating, sand bath heating or high temperature reaction kettle. any kind.

其中,步骤(1)中所述的还原剂为硼氢化钠、硼氢化钾、水合肼、甲酸、乙酸中的任意一种或几种的组合;所述的干燥是在真空或惰性气体保护下加热至50~120摄氏度干燥12小时;所述的惰性气体为氮气、氦气、氩气中的任意一种或几种的组合。Wherein, the reducing agent described in step (1) is any one or a combination of several in sodium borohydride, potassium borohydride, hydrazine hydrate, formic acid, acetic acid; Described drying is under vacuum or inert gas protection Heating to 50-120 degrees Celsius and drying for 12 hours; the inert gas is any one or a combination of nitrogen, helium and argon.

其中,步骤(2)中所述的高温煅烧程序分为两个步骤:第一步是在20~350摄氏度通入还原性气体,煅烧的温度为250~350摄氏度,煅烧时间0.1~10小时;第二步是在350~1000摄氏度通入氨气与惰性气体的混合气,煅烧的温度为500~1000摄氏度,煅烧时间0.1~10小时,混合气中氨气的比例任意且不为零;所述的还原性气体为氢气与惰性气体的混合气,其中氢气的比例任意且不为零;所述的惰性气体为氮气、氦气、氩气中的任意一种或几种的组合。Wherein, the high-temperature calcination procedure described in step (2) is divided into two steps: the first step is to introduce reducing gas at 20~350 degrees Celsius, the calcination temperature is 250~350 degrees Celsius, and the calcination time is 0.1~10 hours; The second step is to introduce a mixture of ammonia gas and inert gas at 350 to 1000 degrees Celsius, the calcination temperature is 500 to 1000 degrees Celsius, the calcination time is 0.1 to 10 hours, and the proportion of ammonia in the mixture is arbitrary and not zero; The reducing gas is a mixture of hydrogen and an inert gas, wherein the proportion of hydrogen is arbitrary and not zero; the inert gas is any one or a combination of nitrogen, helium, and argon.

其中,步骤(3)中所述的去合金化是通过电化学和酸洗的方式实现。Wherein, the dealloying described in step (3) is realized by means of electrochemistry and pickling.

与现有技术相比,本发明具有如下有益效果:Compared with the prior art, the present invention has the following beneficial effects:

本发明技术方案通过调节金属前驱体的比例和高温煅烧工艺来共同实现调控催化剂中的氮含量并控制壳层厚度,所得催化剂形貌均匀,具有良好的催化活性和电化学稳定性,可大幅度降低质子交换膜燃料电池的成本。在0.1摩尔/升饱和氧高氯酸溶液中,本发明的催化剂在0.9伏的氧还原质量活性是商业20wt%Pt/C催化剂的5~19倍,该方法制备的催化剂具有更高的氧还原催化性能,为质子交换膜燃料电池的大规模应用奠定了技术基础。The technical scheme of the present invention realizes the regulation of the nitrogen content in the catalyst and the control of the thickness of the shell layer by adjusting the ratio of the metal precursor and the high-temperature calcination process. The obtained catalyst has a uniform morphology, good catalytic activity and electrochemical stability, and can be greatly Reduce the cost of proton exchange membrane fuel cells. In 0.1 mol/L saturated oxygen perchloric acid solution, the oxygen reduction mass activity of the catalyst of the present invention at 0.9 V is 5-19 times that of the commercial 20wt% Pt/C catalyst, and the catalyst prepared by this method has higher oxygen reduction The catalytic performance has laid a technical foundation for the large-scale application of proton exchange membrane fuel cells.

附图说明Description of drawings

图1为本发明制备方法工艺流程图。Fig. 1 is the process flow diagram of the preparation method of the present invention.

图2为本发明实施例1、实施例2、实施例3制备所得铂铁钼体系催化剂的X射线衍射图。2 is an X-ray diffraction diagram of the platinum-iron-molybdenum system catalyst prepared in Example 1, Example 2, and Example 3 of the present invention.

图3为在0.1摩尔/升饱和氧高氯酸溶液中,本发明实施例1、实施例2、实施例3制备所得铂铁钼体系催化剂和商业20wt%Pt/C催化剂在0.9伏的氧还原质量活性的对比图。Figure 3 shows the oxygen reduction of the platinum-iron-molybdenum system catalyst and commercial 20wt% Pt/C catalyst prepared in Example 1, Example 2, and Example 3 of the present invention at 0.9 volts in a 0.1 mol/L saturated oxygen perchloric acid solution Comparison chart of mass activity.

具体实施方式Detailed ways

下面结合附图具体实施方式进行详细描述,但应当理解本发明的保护范围并不受具体实施方式的限制。The following will describe in detail the specific embodiments in conjunction with the accompanying drawings, but it should be understood that the protection scope of the present invention is not limited by the specific embodiments.

实施例1Example 1

一种氮掺杂双壳层结构纳米催化剂的制备方法,操作步骤如下:A preparation method of a nitrogen-doped double-shell structure nanocatalyst, the operation steps are as follows:

(1)催化剂的还原:取2毫升浓度42毫克/毫升的氯铂酸水溶液,19毫克的三氯化铁和12毫克的七钼酸铵溶于50毫升的去离子水中,即得金属前驱体溶液,然后向金属前驱体溶液中加入200毫克碳黑,超声搅拌分散得到悬浊液,然后将其移至50摄氏度的恒温油浴锅中磁力搅拌,接着加入27毫克的硼氢化钠还原24小时,过滤并用去离子水清洗,所得滤渣在60摄氏度真空干燥12小时得到固体粉末,即为初级产品;(1) reduction of catalyst: take 2 ml of chloroplatinic acid aqueous solution with a concentration of 42 mg/ml, dissolve 19 mg of ferric chloride and 12 mg of ammonium heptamolybdate in 50 ml of deionized water, and obtain metal precursors solution, then add 200 mg of carbon black to the metal precursor solution, ultrasonically stir and disperse to obtain a suspension, then move it to a constant temperature oil bath at 50 degrees Celsius with magnetic stirring, and then add 27 mg of sodium borohydride for reduction for 24 hours , filtered and washed with deionized water, and the obtained filter residue was vacuum-dried at 60 degrees Celsius for 12 hours to obtain solid powder, which was the primary product;

(2)催化剂的高温煅烧:将步骤(1)中所得初级产品置于坩埚中,放入高温反应管式炉中,先通入氢气体积分数为5%的氢气/氩气混合气体,以每分钟5摄氏度的速度从室温加热到300摄氏度,然后保温煅烧1小时;接着通入氨气,以每分钟5摄氏度的速度从300摄氏度加热到600摄氏度,然后保温煅烧1小时,自然冷却至室温,得到氮掺杂的纳米合金催化剂;(2) High-temperature calcination of the catalyst: the primary product obtained in step (1) is placed in a crucible, placed in a high-temperature reaction tube furnace, and a hydrogen/argon mixed gas with a hydrogen volume fraction of 5% is introduced first, with each Heat from room temperature to 300 degrees Celsius at a rate of 5 degrees Celsius per minute, then keep calcined for 1 hour; then feed ammonia gas, heat from 300 degrees Celsius to 600 degrees Celsius at a speed of 5 degrees Celsius per minute, then keep calcined for 1 hour, and naturally cool to room temperature, A nitrogen-doped nano-alloy catalyst is obtained;

(3)去合金化处理:将步骤(2)所得氮掺杂的纳米合金催化剂置于0.5摩尔/升的硫酸溶液中搅拌4小时,然后步骤(1)中的过滤、清洗、干燥步骤,即得氮掺杂双壳层结构的MoN@Fe1@Pt3/C纳米催化剂。(3) dealloying treatment: the nitrogen-doped nano-alloy catalyst obtained in step (2) is placed in a 0.5 mol/L sulfuric acid solution and stirred for 4 hours, and then the filtration, cleaning and drying steps in step (1) are: MoN@Fe 1 @Pt 3 /C nanocatalysts with nitrogen-doped double-shell structure were obtained.

实施例2Example 2

一种氮掺杂双壳层结构纳米催化剂的制备方法,操作步骤如下:A preparation method of a nitrogen-doped double-shell structure nanocatalyst, the operation steps are as follows:

(1)催化剂的还原:取1.7毫升浓度42毫克/毫升的氯铂酸水溶液,48毫克的三氯化铁和11毫克的七钼酸铵溶于50毫升的去离子水中,即得金属前驱体溶液,然后向金属前驱体溶液中加入200毫克碳黑,超声搅拌分散得到悬浊液,然后将其移至50摄氏度的恒温油浴锅中磁力搅拌,接着加入32毫克的硼氢化钠还原24小时,过滤并用去离子水清洗,所得滤渣在60摄氏度真空干燥12小时得到固体粉末,即为初级产品;(1) Reduction of catalyst: take 1.7 ml of chloroplatinic acid aqueous solution with a concentration of 42 mg/ml, 48 mg of ferric chloride and 11 mg of ammonium heptamolybdate and dissolve in 50 ml of deionized water to obtain metal precursors solution, then add 200 mg of carbon black to the metal precursor solution, ultrasonically stir and disperse to obtain a suspension, then move it to a constant temperature oil bath at 50 degrees Celsius with magnetic stirring, and then add 32 mg of sodium borohydride for reduction for 24 hours , filtered and washed with deionized water, and the obtained filter residue was vacuum-dried at 60 degrees Celsius for 12 hours to obtain solid powder, which was the primary product;

(2)催化剂的高温煅烧:将步骤(1)中所得初级产品置于坩埚中,放入高温反应管式炉中,先通入氢气体积分数为5%的氢气/氩气混合气体,以每分钟5摄氏度的速度从室温加热到300摄氏度,然后保温煅烧1小时;接着通入氨气,以每分钟5摄氏度的速度从300摄氏度加热到600摄氏度,然后保温煅烧1小时,自然冷却至室温,得到氮掺杂的纳米合金催化剂;(2) High-temperature calcination of the catalyst: the primary product obtained in step (1) is placed in a crucible, placed in a high-temperature reaction tube furnace, and a hydrogen/argon mixed gas with a hydrogen volume fraction of 5% is introduced first, with each Heat from room temperature to 300 degrees Celsius at a rate of 5 degrees Celsius per minute, then keep calcined for 1 hour; then feed ammonia gas, heat from 300 degrees Celsius to 600 degrees Celsius at a speed of 5 degrees Celsius per minute, then keep calcined for 1 hour, and naturally cool to room temperature, A nitrogen-doped nano-alloy catalyst is obtained;

(3)去合金化处理:将步骤(2)所得氮掺杂的纳米合金催化剂置于0.5摩尔/升的硫酸溶液中搅拌4小时,然后步骤(1)中的过滤、清洗、干燥步骤,即得氮掺杂双壳层结构的MoN@Fe3@Pt3/C纳米催化剂。(3) dealloying treatment: the nitrogen-doped nano-alloy catalyst obtained in step (2) is placed in a 0.5 mol/L sulfuric acid solution and stirred for 4 hours, and then the filtration, cleaning and drying steps in step (1) are: MoN@Fe 3 @Pt 3 /C nanocatalysts with nitrogen-doped double-shell structure were obtained.

实施例3Example 3

一种氮掺杂双壳层结构纳米催化剂的制备方法,操作步骤如下:A preparation method of a nitrogen-doped double-shell structure nanocatalyst, the operation steps are as follows:

(1)催化剂的还原:取1.5毫升浓度42毫克/毫升的氯铂酸水溶液,71毫克的三氯化铁和9毫克的七钼酸铵溶于50毫升的去离子水中,即得金属前驱体溶液,然后向金属前驱体溶液中加入200毫克碳黑,超声搅拌分散得到悬浊液,然后将其移至50摄氏度的恒温油浴锅中磁力搅拌,接着加入37毫克的硼氢化钠还原24小时,过滤并用去离子水清洗,所得滤渣在60摄氏度真空干燥12小时得到固体粉末,即为初级产品;(1) reduction of catalyst: take 1.5 ml of chloroplatinic acid aqueous solution with a concentration of 42 mg/ml, 71 mg of ferric chloride and 9 mg of ammonium heptamolybdate and dissolve in 50 ml of deionized water to obtain metal precursors solution, then add 200 mg of carbon black to the metal precursor solution, ultrasonically stir and disperse to obtain a suspension, then move it to a constant temperature oil bath at 50 degrees Celsius with magnetic stirring, and then add 37 mg of sodium borohydride for reduction for 24 hours , filtered and washed with deionized water, and the obtained filter residue was vacuum-dried at 60 degrees Celsius for 12 hours to obtain solid powder, which was the primary product;

(2)催化剂的高温煅烧:将步骤(1)中所得初级产品置于坩埚中,放入高温反应管式炉中,先通入氢气体积分数为5%的氢气/氩气混合气体,以每分钟5摄氏度的速度从室温加热到300摄氏度,然后保温煅烧1小时;接着通入氨气,以每分钟5摄氏度的速度从300摄氏度加热到600摄氏度,然后保温煅烧1小时,自然冷却至室温,得到氮掺杂的纳米合金催化剂;(2) High-temperature calcination of the catalyst: the primary product obtained in step (1) is placed in a crucible, placed in a high-temperature reaction tube furnace, and a hydrogen/argon mixed gas with a hydrogen volume fraction of 5% is introduced first, with each Heat from room temperature to 300 degrees Celsius at a rate of 5 degrees Celsius per minute, then keep calcined for 1 hour; then feed ammonia gas, heat from 300 degrees Celsius to 600 degrees Celsius at a speed of 5 degrees Celsius per minute, then keep calcined for 1 hour, and naturally cool to room temperature, A nitrogen-doped nano-alloy catalyst is obtained;

(3)去合金化处理:将步骤(2)所得氮掺杂的纳米合金催化剂置于0.5摩尔/升的硫酸溶液中搅拌4小时,然后步骤(1)中的过滤、清洗、干燥步骤,即得氮掺杂双壳层结构的MoN@Fe5@Pt3/C纳米催化剂。(3) dealloying treatment: the nitrogen-doped nano-alloy catalyst obtained in step (2) is placed in a 0.5 mol/L sulfuric acid solution and stirred for 4 hours, and then the filtration, cleaning and drying steps in step (1) are: MoN@Fe 5 @Pt 3 /C nanocatalysts with nitrogen-doped double-shell structure were obtained.

实施例4Example 4

一种氮掺杂双壳层结构纳米催化剂的制备方法,操作步骤如下:A preparation method of a nitrogen-doped double-shell structure nanocatalyst, the operation steps are as follows:

(1)催化剂的还原:取16.4毫升浓度20毫克/毫升的四氯化铂水溶液,23毫克的氯化钴和11毫克的偏钒酸铵溶于50毫升的去离子水中,即得金属前驱体溶液,然后向金属前驱体溶液中加入50毫克氧化石墨烯,超声搅拌分散得到悬浊液,然后将其移至40摄氏度的恒温水浴锅中磁力搅拌,接着加入131毫克的硼氢化钾还原100小时,过滤并用去离子水清洗,所得滤渣在80摄氏度真空干燥12小时得到固体粉末,即为初级产品;(1) reduction of catalyst: take 16.4 ml of platinum tetrachloride aqueous solution with a concentration of 20 mg/ml, dissolve 23 mg of cobalt chloride and 11 mg of ammonium metavanadate in 50 ml of deionized water to obtain a metal precursor solution, then add 50 mg of graphene oxide to the metal precursor solution, ultrasonically stir and disperse to obtain a suspension, then move it to a constant temperature water bath at 40 degrees Celsius with magnetic stirring, and then add 131 mg of potassium borohydride for reduction for 100 hours , filtered and washed with deionized water, and the obtained filter residue was vacuum-dried at 80 degrees Celsius for 12 hours to obtain solid powder, which was the primary product;

(2)催化剂的高温煅烧:将步骤(1)中所得初级产品置于坩埚中,放入高温反应管式炉中,先通入氢气体积分数为5%的氢气/氩气混合气体,以每分钟5摄氏度的速度从室温加热到250摄氏度,然后保温煅烧10小时;接着通入氨气,以每分钟5摄氏度的速度从250摄氏度加热到500摄氏度,然后保温煅烧10小时,自然冷却至室温,得到氮掺杂的纳米合金催化剂;(2) High-temperature calcination of the catalyst: the primary product obtained in step (1) is placed in a crucible, placed in a high-temperature reaction tube furnace, and a hydrogen/argon mixed gas with a hydrogen volume fraction of 5% is introduced first, with each Heat from room temperature to 250 degrees Celsius at a speed of 5 degrees Celsius per minute, and then keep calcined for 10 hours; then feed ammonia gas, heat from 250 degrees Celsius to 500 degrees Celsius at a speed of 5 degrees Celsius per minute, then keep calcined for 10 hours, and naturally cool to room temperature, A nitrogen-doped nano-alloy catalyst is obtained;

(3)去合金化处理:将步骤(2)所得氮掺杂的纳米合金催化剂置于0.5摩尔/升的硫酸溶液中搅拌6小时,然后步骤(1)中的过滤、清洗、干燥步骤,即得氮掺杂双壳层结构的VN@Co1@Pt10/Graphene纳米催化剂。(3) dealloying treatment: the nitrogen-doped nano-alloy catalyst obtained in step (2) is placed in a 0.5 mol/L sulfuric acid solution and stirred for 6 hours, and then the filtration, cleaning and drying steps in step (1) are: The VN@Co 1 @Pt 10 /Graphene nanocatalyst with nitrogen-doped double-shell structure was obtained.

实施例5Example 5

一种氮掺杂双壳层结构纳米催化剂的制备方法,操作步骤如下:A preparation method of a nitrogen-doped double-shell structure nanocatalyst, the operation steps are as follows:

(1)催化剂的还原:取0.8毫升浓度2.5毫克/毫升的氯化钯水溶液,63毫克的三氯化铁和20毫克的七钼酸铵溶于50毫升的去离子水中,即得金属前驱体溶液,然后向金属前驱体溶液中加入225毫克碳纳米管,超声搅拌分散得到悬浊液,然后将其移至200摄氏度的恒温沙浴锅中磁力搅拌,接着加入40毫克的硼氢化钾还原0.1小时,过滤并用去离子水清洗,所得滤渣在120摄氏度真空干燥12小时得到固体粉末,即为初级产品;(1) reduction of catalyst: take 0.8 ml of palladium chloride aqueous solution with a concentration of 2.5 mg/ml, dissolve 63 mg of ferric chloride and 20 mg of ammonium heptamolybdate in 50 ml of deionized water to obtain metal precursors solution, then add 225 mg of carbon nanotubes to the metal precursor solution, ultrasonically stir and disperse to obtain a suspension, then move it to a constant temperature sand bath at 200 degrees Celsius with magnetic stirring, and then add 40 mg of potassium borohydride to reduce 0.1 hour, filter and wash with deionized water, and the obtained filter residue is vacuum-dried at 120 degrees Celsius for 12 hours to obtain solid powder, which is the primary product;

(2)催化剂的高温煅烧:将步骤(1)中所得初级产品置于坩埚中,放入高温反应管式炉中,先通入氢气体积分数为5%的氢气/氩气混合气体,以每分钟5摄氏度的速度从室温加热到350摄氏度,然后保温煅烧0.1小时;接着通入氨气,以每分钟5摄氏度的速度从350摄氏度加热到1000摄氏度,然后保温煅烧0.1小时,自然冷却至室温,得到氮掺杂的纳米合金催化剂;(2) High-temperature calcination of the catalyst: the primary product obtained in step (1) is placed in a crucible, placed in a high-temperature reaction tube furnace, and a hydrogen/argon mixed gas with a hydrogen volume fraction of 5% is introduced first, with each Heat from room temperature to 350 degrees Celsius at a rate of 5 degrees Celsius per minute, and then keep calcined for 0.1 hour; then introduce ammonia gas, heat from 350 degrees Celsius to 1000 degrees Celsius at a speed of 5 degrees Celsius per minute, then keep calcined for 0.1 hour, and naturally cool to room temperature, A nitrogen-doped nano-alloy catalyst is obtained;

(3)去合金化处理:将步骤(2)所得氮掺杂的纳米合金催化剂置于0.5摩尔/升的硫酸溶液中搅拌12小时,然后步骤(1)中的过滤、清洗、干燥步骤,即得氮掺杂双壳层结构的MoN@Fe20@Pd1/CNTs纳米催化剂。(3) dealloying treatment: the nitrogen-doped nano-alloy catalyst obtained in step (2) is placed in a 0.5 mol/L sulfuric acid solution and stirred for 12 hours, and then the filtration, cleaning and drying steps in step (1) are: MoN@Fe 20 @Pd 1 /CNTs nanocatalysts with nitrogen-doped double-shell structure were obtained.

实施例6Example 6

一种氮掺杂双壳层结构纳米催化剂的制备方法,操作步骤如下:A preparation method of a nitrogen-doped double-shell structure nanocatalyst, the operation steps are as follows:

(1)催化剂的还原:取1.3毫升浓度2.5毫克/毫升的硫酸钯水溶液,7毫克的乙酸镍和15毫克的钨酸铵溶于50毫升的去离子水中,即得金属前驱体溶液,然后向金属前驱体溶液中加入237毫克活性炭,超声搅拌分散得到悬浊液,然后将其移至90摄氏度的水浴锅中磁力搅拌,接着加入6毫克的硼氢化钠还原2小时,过滤并用去离子水清洗,所得滤渣在50摄氏度真空干燥12小时得到固体粉末,即为初级产品;(1) reduction of catalyst: take 1.3 ml of palladium sulfate aqueous solution with a concentration of 2.5 mg/ml, dissolve 7 mg of nickel acetate and 15 mg of ammonium tungstate in 50 ml of deionized water to obtain a metal precursor solution, and then add it to Add 237 mg of activated carbon to the metal precursor solution, ultrasonically stir and disperse to obtain a suspension, then move it to a water bath at 90 degrees Celsius with magnetic stirring, then add 6 mg of sodium borohydride to reduce for 2 hours, filter and rinse with deionized water , the obtained filter residue is vacuum-dried at 50 degrees Celsius for 12 hours to obtain solid powder, which is the primary product;

(2)催化剂的高温煅烧:将步骤(1)中所得初级产品置于坩埚中,放入高温反应管式炉中,先通入氢气体积分数为5%的氢气/氩气混合气体,以每分钟5摄氏度的速度从室温加热到300摄氏度,然后保温煅烧1小时;接着通入氨气,以每分钟5摄氏度的速度从300摄氏度加热到800摄氏度,然后保温煅烧5小时,自然冷却至室温,得到氮掺杂的纳米合金催化剂;(2) High-temperature calcination of the catalyst: the primary product obtained in step (1) is placed in a crucible, placed in a high-temperature reaction tube furnace, and a hydrogen/argon mixed gas with a hydrogen volume fraction of 5% is introduced first, with each Heat from room temperature to 300 degrees Celsius at a rate of 5 degrees Celsius per minute, then keep calcined for 1 hour; then feed ammonia gas, heat from 300 degrees Celsius to 800 degrees Celsius at a rate of 5 degrees Celsius per minute, then keep calcined for 5 hours, and naturally cool to room temperature, A nitrogen-doped nano-alloy catalyst is obtained;

(3)去合金化处理:将步骤(2)所得氮掺杂的纳米合金催化剂置于0.5摩尔/升的硫酸溶液中搅拌24小时,然后步骤(1)中的过滤、清洗、干燥步骤,即得氮掺杂双壳层结构的W20N@Ni1@Pd1/活性炭纳米催化剂。(3) dealloying treatment: the nitrogen-doped nano-alloy catalyst obtained in step (2) is placed in a 0.5 mol/L sulfuric acid solution and stirred for 24 hours, and then the filtration, cleaning and drying steps in step (1) are: A nitrogen-doped double-shell structure W 20 N@Ni 1 @Pd 1 /activated carbon nanocatalyst was obtained.

所得氮掺杂双壳层结构纳米催化剂的电化学性能测试:Electrochemical performance test of the obtained nitrogen-doped double-shell nanocatalyst:

(1)分别称取5毫克本发明实施例1~实施例3制备的催化剂和5毫克商业20wt%Pt/C催化剂,分别放入1毫升的Nafion溶液中,所述Nafion溶液由20微升购自杜邦公司的5wt%Nafion溶液和980微升乙醇混合配制而得,超声15分钟,然后用进样器取10微升的浆液滴在旋转圆盘电极上,待干燥后用PINE电化学工作站进行电化学测试。(1) Weigh 5 mg of catalysts prepared in Examples 1 to 3 of the present invention and 5 mg of commercial 20wt% Pt/C catalysts, respectively, and put them into 1 ml of Nafion solution, which was purchased from 20 microliters of Nafion solution. It was prepared by mixing 5wt% Nafion solution of DuPont and 980 μl ethanol, ultrasonicated for 15 minutes, and then used a sampler to take 10 μl of slurry droplets on the rotating disk electrode. After drying, use the PINE electrochemical workstation to carry out Electrochemical testing.

(2)测试条件均如下:碳棒作为对电极,银/氯化银电极作为参比电极,圆盘电极作为工作电极,组成三电极测试体系,以0.1摩尔/升的高氯酸水溶液为电解液。(2) The test conditions are as follows: the carbon rod is used as the counter electrode, the silver/silver chloride electrode is used as the reference electrode, and the disc electrode is used as the working electrode to form a three-electrode test system. liquid.

图2是本发明实施例1~实施例3制备所的铂铁钼体系催化剂的X射线衍射图。2 is an X-ray diffraction diagram of the platinum-iron-molybdenum system catalyst prepared in Examples 1 to 3 of the present invention.

图3是本发明实施例1~实施例3制备所的铂铁钼体系催化剂和商业20wt%Pt/C催化剂在0.9伏的氧还原质量活性的对比图;从图3中我们可以看出,本发明制备所得催化剂具有优良的氧还原催化活性,在0.1摩尔/升饱和氧高氯酸溶液中,本发明的催化剂在0.9伏的氧还原质量活性是商业20wt%Pt/C催化剂的5~19倍,可大幅度降低质子交换膜燃料电池的成本。Figure 3 is a comparison chart of the oxygen reduction mass activity of the platinum-iron-molybdenum system catalyst prepared in Examples 1 to 3 of the present invention and a commercial 20wt% Pt/C catalyst at 0.9 volts; from Figure 3, we can see that this The catalyst prepared by the invention has excellent oxygen reduction catalytic activity. In a 0.1 mol/liter saturated oxygen perchloric acid solution, the oxygen reduction mass activity of the catalyst of the invention at 0.9 volts is 5-19 times that of a commercial 20wt% Pt/C catalyst. , which can greatly reduce the cost of proton exchange membrane fuel cells.

前述对本发明的具体示例性实施方案的描述是为了说明和例证的目的。这些描述并非想将本发明限定为所公开的精确形式,并且很显然,根据上述教导,可以进行很多改变和变化。对示例性实施例进行选择和描述的目的在于解释本发明的特定原理及其实际应用,从而使得本领域的技术人员能够实现并利用本发明的各种不同的示例性实施方案以及各种不同的选择和改变。本发明的范围意在由权利要求书及其等同形式所限定。The foregoing descriptions of specific exemplary embodiments of the present invention have been presented for purposes of illustration and description. These descriptions are not intended to limit the invention to the precise form disclosed, and obviously many changes and modifications are possible in light of the above teachings. The exemplary embodiments were chosen and described for the purpose of explaining certain principles of the invention and their practical applications, to thereby enable one skilled in the art to make and utilize various exemplary embodiments and various different aspects of the invention. Choose and change. The scope of the invention is intended to be defined by the claims and their equivalents.

Claims (6)

1. A preparation method of a nitrogen-doped double-shell structure nano catalyst is characterized by comprising the following operation steps:
(1) and (3) reduction of the catalyst: adding a carrier and a metal precursor into a solvent, stirring, adding a reducing agent, heating to 40-200 ℃, reducing for 0.1-100 hours, filtering, cleaning and drying a mixture obtained by reduction to obtain a primary product; the carrier is any one or combination of a plurality of carbon black, carbon nano tubes, carbon fibers, carbon nano rods, graphene oxide, reduced graphene oxide, activated carbon and porous carbon; wherein, the metal precursor combination mode comprises the following steps: platinum iron tungsten, platinum iron molybdenum, platinum iron vanadium, platinum cobalt tungsten, platinum cobalt molybdenum, platinum cobalt vanadium, platinum nickel tungsten, platinum nickel molybdenum, platinum nickel vanadium, palladium iron tungsten, palladium iron molybdenum, palladium iron vanadium, palladium cobalt tungsten, palladium cobalt molybdenum, palladium cobalt vanadium, palladium nickel tungsten, palladium nickel molybdenum, palladium nickel vanadium, platinum iron cobalt, platinum iron nickel, platinum cobalt nickel, platinum tungsten molybdenum, platinum tungsten vanadium, platinum molybdenum vanadium, palladium iron cobalt, palladium iron nickel, palladium cobalt nickel, palladium tungsten molybdenum, palladium tungsten vanadium, palladium molybdenum vanadium, platinum palladium iron, platinum palladium cobalt, platinum palladium nickel, platinum palladium tungsten, platinum palladium molybdenum or platinum palladium vanadium; the molar ratio of the three elements in the combination is 1-10: 1-20; the platinum is a platinum salt, and the platinum salt is acetylacetone platinum, ammonium hexachloroplatinate, potassium hexachloroplatinate, sodium hexachloroplatinate, potassium tetrachloroplatinate, sodium chloroplatinate, platinum tetrachloride, platinum nitrate, platinum tetraammine nitrate or platinum tetraammine chloride; the palladium is a palladium salt which is palladium chloride, palladium acetate, ammonium chloropalladite, potassium chloropalladite, palladium sulfate, palladium nitrate, sodium tetrachloropalladate, potassium tetrabromopaalladite, palladium dibromide, palladium trifluoroacetate, palladium acetylacetonate, dichlorodiammine palladium, tetraaminopalladium nitrate, palladium hexafluoroacetylacetonate, palladium triphenylphosphine acetate, tetrakis (triphenylphosphine) palladium, bis (benzonitrile) palladium dichloride, bis (triphenylphosphine) palladium chloride, tris (benzylideneacetone) dipalladium, bis (dibenzylideneacetone) palladium, tris (dibenzylideneacetone) dipalladium, (1, 5-cyclooctadiene) palladium dichloride, (1, 3-bis (diphenylphosphino) propane) palladium chloride or 1, 2-bis (diphenylphosphino) ethane palladium dichloride; the iron is ferric salt, and the ferric salt is ferric chloride, ferrous chloride, ferric acetylacetonate, potassium ferricyanide, sodium ferrocyanide, sodium nitrosoferrocyanide, ferrocene, ferric nitrate, ferric citrate, ferric ammonium oxalate, ferrous oxalate, potassium hexacyanoferrate, ferric sulfate, ferrous ammonium sulfate or ferric ammonium sulfate; the cobalt is a cobalt salt, and the cobalt salt is cobalt chloride, cobalt acetate, cobalt phosphate, cobalt phthalocyanine, potassium cobalt cyanide, potassium hexacyanocobaltate, hexaaminocobalt chloride, cobalt perchlorate, cobalt nitrate, cobalt fluoride, cobalt iodide, cobalt bromide, cobalt sodium nitrite, cobalt oxalate, cobalt sulfate, cobaltous sulfate, cobalt ammonium sulfate, cobalt naphthenate or cobalt acetylacetonate; the nickel is nickel salt, and the nickel salt is nickel chloride, nickel acetylacetonate, nickel acetate, nickel bromide, nickel iodide, nickel sulfate, nickel nitrate, nickel ammonium sulfate, nickel hypophosphite, nickel ammonium nitrate, nickel sulfamate, basic nickel carbonate, nickel formate, nickelocene, bis (triphenylphosphine) nickel bromide or bis (triphenylphosphine) nickel chloride; the tungsten is tungsten salt, and the tungsten salt is ammonium metatungstate, ammonium tungstate, potassium tungstate, sodium phosphotungstate, tungsten hexachloride, tungsten hexacarbonyl and tungsten isopropoxide; the molybdenum is molybdenum salt, and the molybdenum salt is ammonium tetramolybdate, ammonium heptamolybdate, ammonium dimolybdate, sodium molybdate, ammonium phosphomolybdate, sodium phosphomolybdate, molybdenum chloride, lithium molybdate, potassium molybdate, molybdenum hexacarbonyl, molybdenum acetylacetonate or molybdenum isopropoxide; the vanadium is a vanadium salt, and the vanadium salt is ammonium metavanadate, sodium metavanadate, potassium metavanadate, sodium orthovanadate, vanadium chloride, vanadium tetrachloride, sodium vanadate, vanadium acetylacetonate, triisopropoxvanadyl, vanadyl acetylacetonate, triisopropoxytriantioxide or vanadyl diacetoneate oxide;
(2) high-temperature calcination of the catalyst: placing the primary product obtained in the step (1) in a high-temperature reaction furnace, and introducing gas for high-temperature calcination to obtain a nitrogen-doped nano alloy catalyst;
the high-temperature calcination procedure is divided into two steps: the first step is that reducing gas is introduced at the temperature of 20-350 ℃, the calcining temperature is 250-350 ℃, and the calcining time is 0.1-10 hours; secondly, introducing a mixed gas of ammonia and inert gas at 350-1000 ℃, wherein the calcining temperature is 500-1000 ℃, the calcining time is 0.1-10 hours, and the proportion of the ammonia in the mixed gas is arbitrary and is not zero; the reducing gas is a mixed gas of hydrogen and inert gas, wherein the proportion of the hydrogen is arbitrary and is not zero; the inert gas is any one or combination of several of nitrogen, helium and argon;
(3) dealloying treatment: and (3) carrying out dealloying treatment on the nitrogen-doped nano alloy catalyst obtained in the step (2) to obtain the nitrogen-doped nano catalyst with a double-shell structure.
2. The method of claim 1, wherein: the solvent in the step (1) is any one or a combination of several of deionized water, ethanol, isopropanol and ethylene glycol.
3. The method of claim 1, wherein: the mass ratio of the carrier in the step (1) to the metal contained in the metal precursor is 0.25-99: 1.
4. The method of claim 1, wherein: the heating mode in the step (1) is any one of water bath heating, oil bath heating, sand bath heating or high-temperature reaction kettle heating.
5. The method of claim 1, wherein: the reducing agent in the step (1) is any one or a combination of several of sodium borohydride, potassium borohydride, hydrazine hydrate, formic acid and acetic acid; the drying is carried out by heating to 50-120 ℃ under vacuum or inert gas protection for 12 hours; the inert gas is any one or combination of several of nitrogen, helium and argon.
6. The method of claim 1, wherein: the dealloying in the step (3) is realized by means of electrochemistry and acid washing.
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