CN115207378B - A kind of polypyrrole nanotube electrocatalyst and its preparation method and application - Google Patents
A kind of polypyrrole nanotube electrocatalyst and its preparation method and application Download PDFInfo
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- 229920000128 polypyrrole Polymers 0.000 title claims abstract description 103
- 239000002071 nanotube Substances 0.000 title claims abstract description 97
- 239000010411 electrocatalyst Substances 0.000 title claims abstract description 65
- 238000002360 preparation method Methods 0.000 title claims abstract description 16
- KAESVJOAVNADME-UHFFFAOYSA-N Pyrrole Chemical compound C=1C=CNC=1 KAESVJOAVNADME-UHFFFAOYSA-N 0.000 claims abstract description 92
- 239000000178 monomer Substances 0.000 claims abstract description 45
- 238000003756 stirring Methods 0.000 claims abstract description 43
- 229910052723 transition metal Inorganic materials 0.000 claims abstract description 40
- 150000003624 transition metals Chemical class 0.000 claims abstract description 27
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 20
- STZCRXQWRGQSJD-GEEYTBSJSA-M methyl orange Chemical compound [Na+].C1=CC(N(C)C)=CC=C1\N=N\C1=CC=C(S([O-])(=O)=O)C=C1 STZCRXQWRGQSJD-GEEYTBSJSA-M 0.000 claims abstract description 19
- 229940012189 methyl orange Drugs 0.000 claims abstract description 19
- 239000000126 substance Substances 0.000 claims abstract description 19
- 229910021578 Iron(III) chloride Inorganic materials 0.000 claims abstract description 18
- RBTARNINKXHZNM-UHFFFAOYSA-K iron trichloride Chemical compound Cl[Fe](Cl)Cl RBTARNINKXHZNM-UHFFFAOYSA-K 0.000 claims abstract description 18
- 229910000314 transition metal oxide Inorganic materials 0.000 claims abstract description 18
- 150000003839 salts Chemical class 0.000 claims abstract description 14
- 238000000034 method Methods 0.000 claims abstract description 12
- -1 transition metal salts Chemical class 0.000 claims abstract description 8
- 238000005292 vacuum distillation Methods 0.000 claims description 16
- 238000001354 calcination Methods 0.000 claims description 13
- 229910021591 Copper(I) chloride Inorganic materials 0.000 claims description 12
- OXBLHERUFWYNTN-UHFFFAOYSA-M copper(I) chloride Chemical compound [Cu]Cl OXBLHERUFWYNTN-UHFFFAOYSA-M 0.000 claims description 12
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 11
- 229910052739 hydrogen Inorganic materials 0.000 claims description 11
- 239000001257 hydrogen Substances 0.000 claims description 11
- 238000006243 chemical reaction Methods 0.000 claims description 7
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 5
- 229910002091 carbon monoxide Inorganic materials 0.000 claims description 5
- 230000000379 polymerizing effect Effects 0.000 claims description 3
- 239000006185 dispersion Substances 0.000 claims 4
- 239000007788 liquid Substances 0.000 claims 4
- 238000004821 distillation Methods 0.000 claims 1
- 229910052759 nickel Inorganic materials 0.000 claims 1
- 230000003197 catalytic effect Effects 0.000 abstract description 12
- 229910052751 metal Inorganic materials 0.000 abstract description 4
- 239000002184 metal Substances 0.000 abstract description 4
- 238000013461 design Methods 0.000 abstract description 2
- 230000007704 transition Effects 0.000 abstract description 2
- 229940032296 ferric chloride Drugs 0.000 description 15
- 238000006116 polymerization reaction Methods 0.000 description 13
- 239000003054 catalyst Substances 0.000 description 12
- 239000008367 deionised water Substances 0.000 description 10
- 229910021641 deionized water Inorganic materials 0.000 description 10
- 238000011065 in-situ storage Methods 0.000 description 10
- 239000007789 gas Substances 0.000 description 6
- 239000000047 product Substances 0.000 description 6
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 5
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 5
- 238000001035 drying Methods 0.000 description 5
- 229940044631 ferric chloride hexahydrate Drugs 0.000 description 5
- NQXWGWZJXJUMQB-UHFFFAOYSA-K iron trichloride hexahydrate Chemical compound O.O.O.O.O.O.[Cl-].Cl[Fe+]Cl NQXWGWZJXJUMQB-UHFFFAOYSA-K 0.000 description 5
- 230000007935 neutral effect Effects 0.000 description 5
- 229910000510 noble metal Inorganic materials 0.000 description 5
- 239000002244 precipitate Substances 0.000 description 5
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- 229910052757 nitrogen Inorganic materials 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 2
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- CKUAXEQHGKSLHN-UHFFFAOYSA-N [C].[N] Chemical compound [C].[N] CKUAXEQHGKSLHN-UHFFFAOYSA-N 0.000 description 1
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- 230000002421 anti-septic effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229910052796 boron Inorganic materials 0.000 description 1
- 150000001721 carbon Chemical class 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
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- 229910052741 iridium Inorganic materials 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 125000004433 nitrogen atom Chemical group N* 0.000 description 1
- 229910052755 nonmetal Inorganic materials 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 230000037361 pathway Effects 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
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- 239000002994 raw material Substances 0.000 description 1
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- 229910052717 sulfur Inorganic materials 0.000 description 1
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- 150000003623 transition metal compounds Chemical class 0.000 description 1
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/90—Selection of catalytic material
- H01M4/9075—Catalytic material supported on carriers, e.g. powder carriers
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M12/00—Hybrid cells; Manufacture thereof
- H01M12/04—Hybrid cells; Manufacture thereof composed of a half-cell of the fuel-cell type and of a half-cell of the primary-cell type
- H01M12/06—Hybrid cells; Manufacture thereof composed of a half-cell of the fuel-cell type and of a half-cell of the primary-cell type with one metallic and one gaseous electrode
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/90—Selection of catalytic material
- H01M4/9041—Metals or alloys
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Abstract
本发明公开一种聚吡咯纳米管电催化剂及其制备方法和应用,该制备方法包括以下步骤:将过渡金属的氧化物或过渡金属的可溶性盐分散于水中,搅拌至完全溶解,得到第一溶液;向第一溶液中加入甲基橙,搅拌至完全溶解,并加入氯化铁,得到第二溶液;向第二溶液中加入吡咯单体,搅拌聚合后,得到包裹有过渡金属氧化物或过渡金属盐的聚吡咯纳米管;将包裹有过渡金属氧化物或过渡金属盐的聚吡咯纳米管在还原性气氛下煅烧,得到包裹有过渡金属单质的聚吡咯纳米管电催化剂。该方法设计合理,操作便捷,得到了兼具良好的催化性能、高比表面积及孔隙率、且气体通道同时具有良好电子导电性以及机械强度的电催化剂。
The invention discloses a polypyrrole nanotube electrocatalyst and its preparation method and application. The preparation method comprises the following steps: dispersing transition metal oxides or transition metal soluble salts in water, stirring until completely dissolved, and obtaining a first solution Add methyl orange to the first solution, stir until completely dissolved, and add ferric chloride to obtain the second solution; add pyrrole monomer to the second solution, stir and polymerize, and obtain a transition metal oxide or transition Polypyrrole nanotubes of metal salts; the polypyrrole nanotubes wrapped with transition metal oxides or transition metal salts are calcined under reducing atmosphere to obtain polypyrrole nanotube electrocatalysts wrapped with transition metal simple substances. The method is reasonable in design and convenient in operation, and an electrocatalyst with good catalytic performance, high specific surface area and porosity, and gas channels with good electronic conductivity and mechanical strength is obtained.
Description
技术领域technical field
本发明属于电池电极材料领域,涉及一种聚吡咯纳米管电催化剂及其制备方法和应用。The invention belongs to the field of battery electrode materials, and relates to a polypyrrole nanotube electrocatalyst and a preparation method and application thereof.
背景技术Background technique
电池作为一种绿色可持续的能源技术顺应了当今社会发展的需求。其中,金属-空气电池具有高理论能量密度、安全性好、成本低、绿色环保等优点而备受关注。金属-空气电池电催化剂电极材料的选用对电池性能至关重要。金属-空气电池的正极电催化剂材料需要实现气体通道和催化剂载体的双重功能,需要具备较高的电子导电性、高比表面积及孔隙率以及较高的机械强度。当前常用的电催化剂为以Pt、Ir等为代表的贵金属催化剂,但贵金属资源稀有,且成本较高,难以工业化应用。过渡金属化合物具有地壳储量丰富、价格便宜、耐碱性强、耐氧化性强等优点,作为一种高效的非贵金属催化剂成为研究热点。然而,这类催化剂目前存在导电性差、催化活性位点暴露率低等缺点,导致催化性能不理想。As a green and sustainable energy technology, batteries meet the needs of today's social development. Among them, metal-air batteries have attracted much attention because of their high theoretical energy density, good safety, low cost, and environmental protection. The selection of electrode materials for electrocatalysts in metal-air batteries is crucial to battery performance. The positive electrode electrocatalyst material for metal-air batteries needs to realize the dual functions of gas channel and catalyst support, and needs to have high electronic conductivity, high specific surface area and porosity, and high mechanical strength. Currently commonly used electrocatalysts are noble metal catalysts represented by Pt, Ir, etc., but noble metal resources are scarce and costly, making it difficult to apply them industrially. Transition metal compounds have the advantages of abundant reserves in the earth's crust, low price, strong alkali resistance, and strong oxidation resistance. As an efficient non-precious metal catalyst, they have become a research hotspot. However, such catalysts currently suffer from disadvantages such as poor electrical conductivity and low exposure of catalytic active sites, resulting in unsatisfactory catalytic performance.
发明内容Contents of the invention
针对现有技术中存在的问题,本发明提供一种聚吡咯纳米管电催化剂及其制备方法和应用,聚吡咯作为一种导电聚合物具有良好导电性从而有利于电子传输,管状结构提供了高比表面积,增加了催化活性位点。从而得到一种兼具良好的催化性能、高比表面积及孔隙率、且气体通道同时具有良好电子导电性以及机械强度的电催化剂。Aiming at the problems existing in the prior art, the present invention provides a polypyrrole nanotube electrocatalyst and its preparation method and application. As a conductive polymer, polypyrrole has good electrical conductivity which is beneficial to electron transport, and the tubular structure provides high The specific surface area increases the catalytically active sites. Therefore, an electrocatalyst with good catalytic performance, high specific surface area and porosity, and good electronic conductivity and mechanical strength in gas channels is obtained.
本发明是通过以下技术方案来实现:The present invention is achieved through the following technical solutions:
一种聚吡咯纳米管电催化剂的制备方法,包括以下步骤:A preparation method of polypyrrole nanotube electrocatalyst, comprising the following steps:
S1:将过渡金属的氧化物或过渡金属的可溶性盐分散于水中,搅拌至完全溶解,得到第一溶液;S1: Dispersing transition metal oxides or transition metal soluble salts in water, stirring until completely dissolved, to obtain a first solution;
S2:向第一溶液中加入甲基橙,搅拌至完全溶解,并加入氯化铁,得到第二溶液;S2: Add methyl orange to the first solution, stir until completely dissolved, and add ferric chloride to obtain the second solution;
S3:向第二溶液中加入吡咯单体,搅拌聚合后,得到包裹有过渡金属氧化物或过渡金属盐的聚吡咯纳米管;S3: adding pyrrole monomers to the second solution, stirring and polymerizing, obtaining polypyrrole nanotubes wrapped with transition metal oxides or transition metal salts;
S4:将所述包裹有过渡金属氧化物或过渡金属盐的聚吡咯纳米管在还原性气氛下煅烧,得到包裹有过渡金属单质的聚吡咯纳米管电催化剂。S4: Calcining the polypyrrole nanotubes wrapped with a transition metal oxide or transition metal salt in a reducing atmosphere to obtain a polypyrrole nanotube electrocatalyst wrapped with a transition metal simple substance.
优选的,所述过渡金属的氧化物为CoO、CuO、Fe2O3和NiO中的任意一种。Preferably, the transition metal oxide is any one of CoO, CuO, Fe 2 O 3 and NiO.
优选的,所述过渡金属的可溶性盐为CoCl2、CuCl2、FeCl3和NiCl2中的任意一种。Preferably, the soluble salt of transition metal is any one of CoCl 2 , CuCl 2 , FeCl 3 and NiCl 2 .
优选的,所述吡咯单体在加入反应体系前采用减压蒸馏的方式进行提纯处理;减压蒸馏的温度为80℃~100℃,压力为0.08MPa。Preferably, the pyrrole monomer is purified by vacuum distillation before being added to the reaction system; the temperature of the vacuum distillation is 80° C. to 100° C., and the pressure is 0.08 MPa.
优选的,所述还原性气氛包括氢气气氛或者一氧化碳气氛。Preferably, the reducing atmosphere includes a hydrogen atmosphere or a carbon monoxide atmosphere.
优选的,所述煅烧的温度为400~600℃。Preferably, the calcination temperature is 400-600°C.
优选的,所述吡咯单体与所述过渡金属的氧化物或可溶性盐中过渡金属的摩尔比为1:(0.5~2.5)。Preferably, the molar ratio of the pyrrole monomer to the transition metal in the transition metal oxide or soluble salt is 1:(0.5-2.5).
优选的,所述甲基橙的浓度范围为3mmol/L~5mmol/L,所述吡咯单体与所述氯化铁的物质的量的比例为1:(0.5~2.5)。Preferably, the concentration range of the methyl orange is 3mmol/L-5mmol/L, and the ratio of the amount of the pyrrole monomer to the ferric chloride is 1:(0.5-2.5).
上述方法制得的一种聚吡咯纳米管电催化剂,所述聚吡咯纳米管电催化剂的比表面积为600~820m2/g;所述聚吡咯纳米管电催化剂的功率密度为70~154mW·cm-2。A polypyrrole nanotube electrocatalyst prepared by the above method, the specific surface area of the polypyrrole nanotube electrocatalyst is 600-820m2 /g; the power density of the polypyrrole nanotube electrocatalyst is 70-154mW·cm -2 .
上述的制备方法制得的聚吡咯纳米管电催化剂在金属-空气电池中的应用。Application of the polypyrrole nanotube electrocatalyst prepared by the above preparation method in a metal-air battery.
与现有技术相比,本发明具有以下有益的技术效果:Compared with the prior art, the present invention has the following beneficial technical effects:
一种聚吡咯纳米管电催化剂的制备方法,采用甲基橙作为软模板剂,氯化铁作为氧化剂,吡咯单体发生聚合过程制备出聚吡咯纳米管,该管状结构可作为气体通道,提高金属-空气电池电催化剂的催化效率,同时在反应体系中加入过渡金属的氧化物或过渡金属的可溶性盐,在聚吡咯纳米管的合成过程中,使过渡金属的氧化物或过渡金属的可溶性盐原位包裹在聚吡咯纳米管的内部,同时,在还原性气氛下煅烧,得到包裹有过渡金属单质的聚吡咯纳米管,在煅烧过程中聚吡咯纳米管形成更加稳定的氮-碳(N-C)结构,形成了性能良好的(金属-氮-碳)M-N-C型聚吡咯纳米管电催化剂。该方法设计合理,操作便捷,得到了兼具良好的催化性能、高比表面积及孔隙率、且气体通道同时具有良好电子导电性以及机械强度的电催化剂。A method for preparing polypyrrole nanotube electrocatalysts, using methyl orange as a soft template, ferric chloride as an oxidant, and polymerizing pyrrole monomers to prepare polypyrrole nanotubes. The tubular structure can be used as a gas channel to increase metal - Catalytic efficiency of air battery electrocatalysts, while adding transition metal oxides or transition metal soluble salts in the reaction system, in the synthesis process of polypyrrole nanotubes, transition metal oxides or transition metal soluble salts The polypyrrole nanotubes are wrapped in the inside of the polypyrrole nanotubes, and at the same time, they are calcined in a reducing atmosphere to obtain polypyrrole nanotubes wrapped with a transition metal element. During the calcination process, the polypyrrole nanotubes form a more stable nitrogen-carbon (N-C) structure. , forming a (metal-nitrogen-carbon) M-N-C type polypyrrole nanotube electrocatalyst with good performance. The method is reasonable in design and convenient in operation, and an electrocatalyst with good catalytic performance, high specific surface area and porosity, and gas channels with good electronic conductivity and mechanical strength is obtained.
进一步的,吡咯单体在进行聚合反应前采用减压蒸馏的方式进行提纯处理,可以有效减少合成的聚吡咯纳米管的纯度。Further, the pyrrole monomer is purified by vacuum distillation before the polymerization reaction, which can effectively reduce the purity of the synthesized polypyrrole nanotubes.
进一步的,煅烧的温度为400~600℃,一方面确保了聚吡咯纳米管的结构稳定性,另一方面可使得过渡金属的氧化物或过渡金属的可溶性在还原性气氛中被有效还原为过渡金属单质。Further, the calcination temperature is 400-600°C. On the one hand, it ensures the structural stability of polypyrrole nanotubes, and on the other hand, it can effectively reduce the transition metal oxide or transition metal solubility to transition Elemental metal.
附图说明Description of drawings
为了更清楚地说明本发明实施例的技术方案,下面将对实施例中所需要使用的附图作简单地介绍,应当理解,以下附图仅示出了本发明的某些实施例,因此不应被看作是对范围的限定,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据这些附图获得其他相关的附图。In order to illustrate the technical solutions of the embodiments of the present invention more clearly, the accompanying drawings used in the embodiments will be briefly introduced below. It should be understood that the following drawings only show some embodiments of the present invention, and thus It should be regarded as a limitation on the scope, and those skilled in the art can also obtain other related drawings based on these drawings without creative work.
图1为本发明中一种聚吡咯纳米管电催化剂制备方法的流程示意图;Fig. 1 is the schematic flow sheet of a kind of polypyrrole nanotube electrocatalyst preparation method among the present invention;
图2为本发明实施例3制得的聚吡咯纳米管电催化剂在不同放大倍率下SEM图。Fig. 2 is the SEM image of the polypyrrole nanotube electrocatalyst prepared in Example 3 of the present invention under different magnifications.
图3为本发明实施例3制得的聚吡咯纳米管电催化剂的TEM图。3 is a TEM image of the polypyrrole nanotube electrocatalyst prepared in Example 3 of the present invention.
具体实施方式Detailed ways
为使本领域技术人员可了解本发明的特点及效果,以下谨就说明书及权利要求书中提及的术语及用语进行一般性的说明及定义。除非另有指明,否则文中使用的所有技术及科学上的字词,均为本领域技术人员对于本发明所了解的通常意义,当有冲突情形时,应以本说明书的定义为准。In order to enable those skilled in the art to understand the features and effects of the present invention, the terms and terms mentioned in the specification and claims are generally described and defined below. Unless otherwise specified, all technical and scientific terms used herein have the usual meanings understood by those skilled in the art for the present invention. In case of conflict, the definitions in this specification shall prevail.
本文描述和公开的理论或机制,无论是对或错,均不应以任何方式限制本发明的范围,即本发明内容可以在不为任何特定的理论或机制所限制的情况下实施。The theories or mechanisms described and disclosed herein, whether true or false, should not limit the scope of the present invention in any way, ie, the present invention can be practiced without being limited by any particular theory or mechanism.
本文中,所有以数值范围或百分比范围形式界定的特征如数值、数量、含量与浓度仅是为了简洁及方便。据此,数值范围或百分比范围的描述应视为已涵盖且具体公开所有可能的次级范围及范围内的个别数值(包括整数与分数)。Herein, all the features defined in the form of numerical range or percentage range, such as numerical value, quantity, content and concentration, are only for the sake of brevity and convenience. Accordingly, the recitation of a numerical range or a percentage range should be deemed to encompass and specifically disclose all possible subranges and individual values (including integers and fractions) within those ranges.
本文中,若无特别说明,“包含”、“包括”、“含有”、“具有”或类似用语涵盖了“由……组成”和“主要由……组成”的意思,例如“A包含a”涵盖了“A包含a和其他”和“A仅包含a”的意思。In this article, unless otherwise specified, "comprising", "comprising", "comprising", "having" or similar expressions cover the meanings of "consisting of" and "consisting mainly of", for example, "A contains a " covers the meanings of "A contains a and others" and "A contains only a".
本文中,为使描述简洁,未对各个实施方案或实施例中的各个技术特征的所有可能的组合都进行描述。因此,只要这些技术特征的组合不存在矛盾,各个实施方案或实施例中的各个技术特征可以进行任意的组合,所有可能的组合都应当认为是本说明书记载的范围。Herein, for the sake of concise description, all possible combinations of the technical features in each embodiment or embodiment are not described. Therefore, as long as there is no contradiction in the combination of these technical features, each technical feature in each embodiment or example can be combined arbitrarily, and all possible combinations should be regarded as within the scope of this specification.
研究显示,直接使用非贵金属作为电催化剂催化效率低,目前主要通过掺杂来提高催化效率,主要包含过渡金属杂原子共掺杂碳,以及N、B、S、O、P等的杂原子掺杂。目前,在非金属掺杂改性中,由于氮与碳原子尺寸相似,氮原子可掺杂到碳结构的边缘或内部,产生相应的活性位点。因氮掺杂相对其他杂原子掺杂实现过程更容易,且可产生很多相应的活性位点,因此,过渡金属与氮掺杂碳催化剂成为更具有实用价值、更有希望取代贵金属的催化剂,称为过渡金属与氮改性的碳催化剂,简称M-N-C催化剂。这种杂原子改性的碳催化材料因其廉价性、稳定性和良好导电性,被认为是贵金属催化剂的潜在替代品。然而,目前研究中所报道的M-N-C催化剂一方面合成路径较为复杂,同时催化效率不理想的缺点。Studies have shown that the direct use of non-noble metals as electrocatalysts has low catalytic efficiency. At present, the catalytic efficiency is mainly improved by doping, which mainly includes co-doped carbon with transition metal heteroatoms, and heteroatom doped with N, B, S, O, P, etc. miscellaneous. At present, in non-metal doping modification, nitrogen atoms can be doped to the edge or inside of the carbon structure to generate corresponding active sites due to the similar size of nitrogen and carbon atoms. Because nitrogen doping is easier to achieve than other heteroatom doping, and can produce many corresponding active sites, transition metal and nitrogen-doped carbon catalysts have become more practical and promising catalysts to replace noble metals, called It is a transition metal and nitrogen modified carbon catalyst, referred to as M-N-C catalyst. This heteroatom-modified carbon catalytic material is considered as a potential substitute for noble metal catalysts due to its cheapness, stability, and good electrical conductivity. However, the M-N-C catalysts reported in the current study have the disadvantages of complex synthetic pathways and unsatisfactory catalytic efficiency.
本发明选择聚吡咯为基础材料,聚吡咯具备N-C结构分子基础,可有效提高催化剂的电子导电性达到高催化效率。同时,聚吡咯的聚合过程中通过模板剂的诱导,能够实现圆管状、方管状等多种形貌,这些天然的孔道结构,可作为气体通道,提高金属-空气电池电催化剂的催化效率。并且,通过控制反应条件,可调节聚吡咯管孔径大小,因此,本发明通过将聚吡咯纳米管作为过渡金属的负载剂,可以根据实际应用条件调控聚吡咯纳米管的形貌及管径,从而调控催化剂的负载量及气体通量。而聚吡咯本身作为一种导电聚合物,具有高电子电导率、高机械强度的优点,通过控制反应条件,可以制备出具有中空结构的聚吡咯纳米管,达到高比表面积。同时,聚吡咯本身具备防腐性能。由此可见,聚吡咯纳米管是一种兼具多种优良性能的电极电催化剂材料,同时还兼具有良好的防腐性能。The invention selects polypyrrole as the basic material, and the polypyrrole has an N-C structure molecular basis, which can effectively improve the electronic conductivity of the catalyst to achieve high catalytic efficiency. At the same time, through the induction of the template agent in the polymerization process of polypyrrole, various shapes such as circular tubes and square tubes can be realized. These natural pore structures can be used as gas channels to improve the catalytic efficiency of metal-air battery electrocatalysts. And, by controlling the reaction conditions, the pore size of the polypyrrole tube can be adjusted. Therefore, the present invention can regulate the morphology and diameter of the polypyrrole nanotube according to the actual application conditions by using the polypyrrole nanotube as a loading agent for the transition metal, thereby Regulate the loading capacity and gas flux of the catalyst. As a conductive polymer, polypyrrole itself has the advantages of high electronic conductivity and high mechanical strength. By controlling the reaction conditions, polypyrrole nanotubes with a hollow structure can be prepared to achieve a high specific surface area. At the same time, polypyrrole itself has antiseptic properties. It can be seen that polypyrrole nanotubes are an electrode electrocatalyst material with various excellent properties, and also have good anti-corrosion properties.
为了构建上述性能优异的聚吡咯纳米管电催化剂,其制备方法如图1所示,具体为:In order to construct the above-mentioned polypyrrole nanotube electrocatalyst with excellent performance, its preparation method is shown in Figure 1, specifically:
S1:将过渡金属的氧化物或过渡金属的可溶性盐分散于水中,搅拌至完全溶解,得到第一溶液;S1: Dispersing transition metal oxides or transition metal soluble salts in water, stirring until completely dissolved, to obtain a first solution;
其中,过渡金属的氧化物包括CoO、CuO、Fe2O3和NiO中的任意一种。过渡金属的可溶性盐包括CoCl2、CuCl2、FeCl3和NiCl2中的任意一种。吡咯单体与所述过渡金属的氧化物或可溶性盐中过渡金属的摩尔比为1:(0.5~2.5)。Wherein, the transition metal oxide includes any one of CoO, CuO, Fe 2 O 3 and NiO. Soluble salts of transition metals include any one of CoCl 2 , CuCl 2 , FeCl 3 and NiCl 2 . The molar ratio of the pyrrole monomer to the transition metal in the transition metal oxide or soluble salt is 1:(0.5-2.5).
S2:向第一溶液中加入甲基橙,搅拌至完全溶解,并加入氯化铁,得到第二溶液;其中,甲基橙的浓度范围为3mmol/L~5mmol/L。S2: Add methyl orange to the first solution, stir until completely dissolved, and add ferric chloride to obtain a second solution; wherein the concentration of methyl orange is in the range of 3mmol/L-5mmol/L.
S3:向第二溶液中加入吡咯单体,搅拌聚合后,得到包裹有过渡金属氧化物或过渡金属盐的聚吡咯纳米管;其中,吡咯单体与氯化铁的物质的量的比例为1:(0.5~2.5),且吡咯单体在进行聚合反应前采用减压蒸馏的方式进行提纯处理;减压蒸馏的温度为80℃~100℃,压力为0.08MPa。S3: Add pyrrole monomer to the second solution, stir and polymerize, and obtain polypyrrole nanotubes wrapped with transition metal oxide or transition metal salt; wherein, the ratio of the amount of pyrrole monomer to ferric chloride is 1 : (0.5~2.5), and the pyrrole monomer is purified by vacuum distillation before the polymerization reaction; the temperature of vacuum distillation is 80°C-100°C, and the pressure is 0.08MPa.
S4:将所述包裹有过渡金属氧化物或过渡金属盐的聚吡咯纳米管在还原性气氛下煅烧,得到包裹有过渡金属单质的聚吡咯纳米管电催化剂。S4: Calcining the polypyrrole nanotubes wrapped with a transition metal oxide or transition metal salt in a reducing atmosphere to obtain a polypyrrole nanotube electrocatalyst wrapped with a transition metal simple substance.
其中,还原性气氛包括氢气气氛或者一氧化碳气氛;煅烧的温度为400~600℃。Wherein, the reducing atmosphere includes a hydrogen atmosphere or a carbon monoxide atmosphere; the calcining temperature is 400-600°C.
通过上述的方法制得的聚吡咯纳米管电催化剂的管径为80~200nm,比表面积为600~820m2/g;功率密度为70~154mW·cm-2。The diameter of the polypyrrole nanotube electrocatalyst prepared by the above method is 80-200nm, the specific surface area is 600-820m 2 /g, and the power density is 70-154mW·cm -2 .
下面结合具体实施例,进一步阐述本发明。应理解,这些实施例仅用于说明本发明而不用于限制本发明的范围。此外应理解,在阅读了本发明讲授的内容之后,本领域技术人员可以对本发明作各种改动或修改,这些等价形式同样落于本申请所附权利要求书所限定的范围。Below in conjunction with specific embodiment, further illustrate the present invention. It should be understood that these examples are only used to illustrate the present invention and are not intended to limit the scope of the present invention. In addition, it should be understood that after reading the teachings of the present invention, those skilled in the art can make various changes or modifications to the present invention, and these equivalent forms also fall within the scope defined by the appended claims of the present application.
下列实施例中使用本领域常规的仪器设备。下列实施例中未注明具体条件的实验方法,通常按照常规条件,或按照制造厂商所建议的条件。下列实施例中使用各种原料,除非另作说明,都使用常规市售产品,其规格为本领域常规规格。在本发明的说明书以及下述实施例中,如没有特别说明,“%”都表示重量百分比,“份”都表示重量份,比例都表示重量比。Conventional instruments and equipment in the art are used in the following examples. For the experimental methods without specific conditions indicated in the following examples, the conventional conditions or the conditions suggested by the manufacturer are usually followed. Various raw materials are used in the following examples. Unless otherwise specified, conventional commercially available products are used, and their specifications are conventional specifications in the art. In the description of the present invention and the following examples, unless otherwise specified, "%" means weight percentage, "part" means weight part, and ratio means weight ratio.
实施例1Example 1
通过减压蒸馏法对吡咯单体进行提纯,减压蒸馏的温度为80℃、压力为0.08MPa。取0.55g CuCl2分散于300mL去离子水中,常温下搅拌30min,使其完全溶解。取300mg甲基橙溶于300mL上述溶液中,常温下搅拌5h,至溶液变成清澈的桃红色,然后缓慢加入2.22g的六水合三氯化铁,溶液立即出现深红色絮状沉淀。继续快速搅拌50min,再加入1.1g吡咯单体,观察溶液变为黑绿色,通过原位聚合法在室温下(25℃)聚合24h,得到了包裹有CuCl2的聚吡咯纳米管。抽滤,产物用去离子水和无水乙醇反复清洗,除去模板、未反应的吡咯单体和FeCl3·6H2O,直至pH值呈中性,烘干。将烘干后得到的包裹有CuCl2的聚吡咯纳米管置于氢气气氛中,在400℃下煅烧处理,得到包裹有Cu单质的聚吡咯纳米管电催化剂。The pyrrole monomer was purified by vacuum distillation, the temperature of the vacuum distillation was 80° C., and the pressure was 0.08 MPa. Take 0.55g CuCl 2 and disperse it in 300mL deionized water, stir at room temperature for 30min to make it completely dissolve. Dissolve 300mg of methyl orange in 300mL of the above solution, stir at room temperature for 5 hours until the solution turns clear pink, then slowly add 2.22g of ferric chloride hexahydrate, and the solution immediately appears dark red flocculent precipitate. Continue to stir rapidly for 50 min, then add 1.1 g of pyrrole monomer, observe that the solution turns black and green, and polymerize at room temperature (25 ° C) for 24 h by in situ polymerization, and obtain polypyrrole nanotubes wrapped with CuCl 2 . After suction filtration, the product was repeatedly washed with deionized water and absolute ethanol to remove the template, unreacted pyrrole monomer and FeCl 3 ·6H 2 O until the pH value was neutral, and dried. The polypyrrole nanotubes coated with CuCl 2 obtained after drying were placed in a hydrogen atmosphere, and calcined at 400° C. to obtain a polypyrrole nanotube electrocatalyst coated with Cu simple substance.
本实施例制得的包裹有Cu单质的聚吡咯纳米管电催化剂的管径为80nm,比表面积为600m2/g,功率密度为70mW·cm-2。The Cu-wrapped polypyrrole nanotube electrocatalyst prepared in this example has a tube diameter of 80 nm, a specific surface area of 600 m 2 /g, and a power density of 70 mW·cm -2 .
实施例2Example 2
通过减压蒸馏法对吡咯单体进行提纯,减压蒸馏的温度为90℃、压力为0.08MPa。取0.55g CuCl2分散于490mL去离子水中,常温下搅拌30min,使其完全溶解。取300mg甲基橙溶于300mL上述溶液中,常温下搅拌5h,至溶液变成清澈的桃红色,然后缓慢加入2.22g的六水合三氯化铁,溶液立即出现深红色絮状沉淀。继续快速搅拌50min,再加入1.1g吡咯单体,观察溶液变为黑绿色,通过原位聚合法在室温下(25℃)聚合24h,得到了包裹有CuCl2的聚吡咯纳米管。抽滤,产物用去离子水和无水乙醇反复清洗,除去模板、未反应的吡咯单体和FeCl3·6H2O,直至pH值呈中性,烘干。将烘干后得到的包裹有CuCl2的聚吡咯纳米管置于氢气气氛中,在440℃下煅烧处理,得到包裹有Cu单质的聚吡咯纳米管电催化剂。The pyrrole monomer was purified by vacuum distillation, the temperature of vacuum distillation was 90° C., and the pressure was 0.08 MPa. Take 0.55g CuCl 2 and disperse it in 490mL deionized water, stir at room temperature for 30min to make it completely dissolve. Dissolve 300mg of methyl orange in 300mL of the above solution, stir at room temperature for 5 hours until the solution turns clear pink, then slowly add 2.22g of ferric chloride hexahydrate, and the solution immediately appears dark red flocculent precipitate. Continue to stir rapidly for 50 min, then add 1.1 g of pyrrole monomer, observe that the solution turns black and green, and polymerize at room temperature (25 ° C) for 24 h by in situ polymerization, and obtain polypyrrole nanotubes wrapped with CuCl 2 . After suction filtration, the product was repeatedly washed with deionized water and absolute ethanol to remove the template, unreacted pyrrole monomer and FeCl 3 ·6H 2 O until the pH value was neutral, and dried. The polypyrrole nanotubes coated with CuCl 2 obtained after drying were placed in a hydrogen atmosphere, and calcined at 440° C. to obtain a polypyrrole nanotube electrocatalyst coated with Cu simple substance.
本实施例制得的包裹有Cu单质的聚吡咯纳米管电催化剂的管径为100nm,比表面积为700m2/g,功率密度为78mW·cm-2。The Cu-wrapped polypyrrole nanotube electrocatalyst prepared in this example has a tube diameter of 100 nm, a specific surface area of 700 m 2 /g, and a power density of 78 mW·cm -2 .
实施例3Example 3
通过减压蒸馏法对吡咯单体进行提纯,减压蒸馏的温度为100℃、压力为0.08MPa。取0.55g CuCl2分散于490mL去离子水中,常温下搅拌30min,使其完全溶解。取300mg甲基橙溶于300mL上述溶液中,常温下搅拌5h,至溶液变成清澈的桃红色,然后缓慢加入6.65g的六水合三氯化铁,溶液立即出现深红色絮状沉淀。继续快速搅拌50min,再加入1.1g吡咯单体,观察溶液变为黑绿色,通过原位聚合法在室温下(25℃)聚合24h,得到了包裹有CuCl2的聚吡咯纳米管。抽滤,产物用去离子水和无水乙醇反复清洗,除去模板、未反应的吡咯单体和FeCl3·6H2O,直至pH值呈中性,烘干。将烘干后得到的包裹有CuCl2的聚吡咯纳米管置于氢气气氛中,在550℃下煅烧处理,得到包裹有Cu单质的聚吡咯纳米管电催化剂。The pyrrole monomer was purified by vacuum distillation, the temperature of vacuum distillation was 100° C., and the pressure was 0.08 MPa. Take 0.55g CuCl 2 and disperse it in 490mL deionized water, stir at room temperature for 30min to make it completely dissolve. Dissolve 300mg of methyl orange in 300mL of the above solution, stir at room temperature for 5 hours until the solution turns clear pink, then slowly add 6.65g of ferric chloride hexahydrate, and the solution immediately appears dark red flocculent precipitate. Continue to stir rapidly for 50 min, then add 1.1 g of pyrrole monomer, observe that the solution turns black and green, and polymerize at room temperature (25 ° C) for 24 h by in situ polymerization, and obtain polypyrrole nanotubes wrapped with CuCl 2 . After suction filtration, the product was repeatedly washed with deionized water and absolute ethanol to remove the template, unreacted pyrrole monomer and FeCl 3 ·6H 2 O until the pH value was neutral, and dried. The polypyrrole nanotubes coated with CuCl 2 obtained after drying were placed in a hydrogen atmosphere, and calcined at 550° C. to obtain a polypyrrole nanotube electrocatalyst coated with Cu simple substance.
本实施例制得的包裹有Cu单质的聚吡咯纳米管电催化剂的管径为120nm,比表面积为720m2/g,功率密度为80mW·cm-2。The Cu-wrapped polypyrrole nanotube electrocatalyst prepared in this example has a tube diameter of 120 nm, a specific surface area of 720 m 2 /g, and a power density of 80 mW·cm -2 .
本发明制得的包裹有Cu单质的聚吡咯纳米管的SEM图如图2所示,TEM图如图3所示,由图可以看出吡咯纳米管大约在80-200nm,呈现中空管状结构,且内部包裹有过渡金属单质。The SEM picture of the polypyrrole nanotube wrapped with Cu simple substance prepared by the present invention is shown in Figure 2, and the TEM picture is shown in Figure 3. It can be seen from the figure that the pyrrole nanotube is about 80-200nm and presents a hollow tubular structure. And the interior is wrapped with a transition metal element.
实施例4Example 4
通过减压蒸馏法对吡咯单体进行提纯,减压蒸馏的温度为95℃、压力为0.08MPa。取1.65g CoCl2分散于490mL去离子水中,常温下搅拌30min,使其完全溶解。取300mg甲基橙溶于300mL上述溶液中,常温下搅拌5h,至溶液变成清澈的桃红色,然后缓慢加入6.65g的六水合三氯化铁,溶液立即出现深红色絮状沉淀。继续快速搅拌50min,再加入1.1g吡咯单体,观察溶液变为黑绿色,通过原位聚合法在室温下(25℃)聚合24h,得到了包裹有CoCl2的聚吡咯纳米管。抽滤,产物用去离子水和无水乙醇反复清洗,除去模板、未反应的吡咯单体和FeCl3·6H2O,直至pH值呈中性,烘干。将烘干后得到的包裹有CoCl2的聚吡咯纳米管置于氢气气氛中,在450℃下煅烧处理,得到包裹有Co金属单质的聚吡咯纳米管电催化剂。The pyrrole monomer was purified by vacuum distillation, the temperature of the vacuum distillation was 95° C., and the pressure was 0.08 MPa. Take 1.65g CoCl 2 and disperse it in 490mL deionized water, stir at room temperature for 30min to make it completely dissolve. Dissolve 300mg of methyl orange in 300mL of the above solution, stir at room temperature for 5 hours until the solution turns clear pink, then slowly add 6.65g of ferric chloride hexahydrate, and the solution immediately appears dark red flocculent precipitate. Continue to stir rapidly for 50 minutes, then add 1.1 g of pyrrole monomer, observe that the solution turns black and green, and polymerize at room temperature (25° C.) for 24 hours by in-situ polymerization, and obtain polypyrrole nanotubes wrapped with CoCl 2 . After suction filtration, the product was repeatedly washed with deionized water and absolute ethanol to remove the template, unreacted pyrrole monomer and FeCl 3 ·6H 2 O until the pH value was neutral, and dried. The polypyrrole nanotubes coated with CoCl 2 obtained after drying were placed in a hydrogen atmosphere, and calcined at 450 ° C to obtain a polypyrrole nanotube electrocatalyst coated with a Co metal element.
本实施例制得的包裹有Co单质的聚吡咯纳米管电催化剂的管径为140nm,比表面积为750m2/g,功率密度为90mW·cm-2。The polypyrrole nanotube electrocatalyst coated with Co simple substance prepared in this example has a tube diameter of 140 nm, a specific surface area of 750 m 2 /g, and a power density of 90 mW·cm -2 .
实施例5Example 5
通过减压蒸馏法对吡咯单体进行提纯,减压蒸馏的温度为85℃、压力为0.08MPa。取1.65g CoO分散于490mL去离子水中,常温下搅拌30min,使其完全溶解。取300mg甲基橙溶于300mL上述溶液中,常温下搅拌5h,至溶液变成清澈的桃红色,然后缓慢加入6.65g的六水合三氯化铁,溶液立即出现深红色絮状沉淀。继续快速搅拌50min,再加入1.1g吡咯单体,观察溶液变为黑绿色,通过原位聚合法在室温下(25℃)聚合24h,得到了包裹有CoO的聚吡咯纳米管。抽滤,产物用去离子水和无水乙醇反复清洗,除去模板、未反应的吡咯单体和FeCl3·6H2O,直至pH值呈中性,烘干。将烘干后得到的包裹有CoO的聚吡咯纳米管置于氢气气氛中,在470℃下煅烧处理,得到包裹有Co单质的聚吡咯纳米管电催化剂。The pyrrole monomer was purified by vacuum distillation, the temperature of vacuum distillation was 85° C., and the pressure was 0.08 MPa. Take 1.65g CoO and disperse it in 490mL deionized water, stir at room temperature for 30min to make it completely dissolved. Dissolve 300mg of methyl orange in 300mL of the above solution, stir at room temperature for 5 hours until the solution turns clear pink, then slowly add 6.65g of ferric chloride hexahydrate, and the solution immediately appears dark red flocculent precipitate. Continue to stir rapidly for 50 minutes, then add 1.1 g of pyrrole monomer, observe that the solution turns black and green, and polymerize at room temperature (25° C.) for 24 hours by in-situ polymerization, and obtain polypyrrole nanotubes coated with CoO. After suction filtration, the product was repeatedly washed with deionized water and absolute ethanol to remove the template, unreacted pyrrole monomer and FeCl 3 ·6H 2 O until the pH value was neutral, and dried. The polypyrrole nanotubes coated with CoO obtained after drying were placed in a hydrogen atmosphere, and calcined at 470° C. to obtain a polypyrrole nanotube electrocatalyst coated with Co simple substance.
本实施例制得的包裹有Co单质的聚吡咯纳米管电催化剂的管径为160nm,比表面积为780m2/g,功率密度为110mW·cm-2。The polypyrrole nanotube electrocatalyst coated with Co simple substance prepared in this example has a tube diameter of 160 nm, a specific surface area of 780 m 2 /g, and a power density of 110 mW·cm -2 .
实施例6Example 6
一种聚吡咯纳米管电催化剂的制备方法,其特征在于,包括以下步骤:A preparation method of polypyrrole nanotube electrocatalyst, is characterized in that, comprises the following steps:
S1:将CoO分散于水中,搅拌至完全溶解,得到第一溶液;S1: Disperse CoO in water and stir until completely dissolved to obtain the first solution;
S2:向第一溶液中加入3mmol/L甲基橙,搅拌至完全溶解,并加入氯化铁,得到第二溶液;S2: Add 3mmol/L methyl orange to the first solution, stir until completely dissolved, and add ferric chloride to obtain the second solution;
S3:向第二溶液中加入吡咯单体,吡咯单体与氯化铁的物质的量的比例为1:0.5,吡咯单体与Co的摩尔比为1:0.5;搅拌发生原位聚合反应后,得到包裹有CoO的聚吡咯纳米管;S3: Add pyrrole monomer to the second solution, the ratio of the amount of pyrrole monomer to ferric chloride is 1:0.5, and the molar ratio of pyrrole monomer to Co is 1:0.5; after in-situ polymerization occurs after stirring , to obtain polypyrrole nanotubes wrapped with CoO;
S4:将所述包裹有CoO的聚吡咯纳米管置于一氧化碳气氛中,在400℃下煅烧处理,得到包裹有Co单质的聚吡咯纳米管电催化剂。S4: placing the CoO-wrapped polypyrrole nanotubes in a carbon monoxide atmosphere and calcining at 400° C. to obtain a Co-wrapped polypyrrole nanotube electrocatalyst.
本实施例制得的包裹有Co单质的聚吡咯纳米管电催化剂的管径为180nm,比表面积为800m2/g,功率密度为115mW·cm-2。The polypyrrole nanotube electrocatalyst coated with Co simple substance prepared in this example has a tube diameter of 180 nm, a specific surface area of 800 m 2 /g, and a power density of 115 mW·cm -2 .
实施例7Example 7
一种聚吡咯纳米管电催化剂的制备方法,其特征在于,包括以下步骤:A preparation method of polypyrrole nanotube electrocatalyst, is characterized in that, comprises the following steps:
S1:将CuO分散于水中,搅拌至完全溶解,得到第一溶液;S1: Disperse CuO in water and stir until completely dissolved to obtain the first solution;
S2:向第一溶液中加入4mmol/L甲基橙,搅拌至完全溶解,并加入氯化铁,得到第二溶液;S2: Add 4mmol/L methyl orange to the first solution, stir until completely dissolved, and add ferric chloride to obtain the second solution;
S3:向第二溶液中加入吡咯单体,吡咯单体与氯化铁的物质的量的比例为1:1.5,吡咯单体与Cu的摩尔比为1:1;搅拌发生原位聚合反应后,得到包裹有CuO的聚吡咯纳米管;S3: Add pyrrole monomer to the second solution, the ratio of the amount of pyrrole monomer to ferric chloride is 1:1.5, and the molar ratio of pyrrole monomer to Cu is 1:1; after in-situ polymerization occurs after stirring , to obtain polypyrrole nanotubes wrapped with CuO;
S4:将所述包裹有CuO的聚吡咯纳米管置于一氧化碳气氛中,在500℃下煅烧处理,得到包裹有Cu单质的聚吡咯纳米管电催化剂。S4: placing the CuO-wrapped polypyrrole nanotubes in a carbon monoxide atmosphere, and calcining them at 500° C. to obtain a Cu-wrapped polypyrrole nanotube electrocatalyst.
本实施例制得的包裹有Cu单质的聚吡咯纳米管电催化剂的管径为190nm,比表面积为820m2/g,功率密度为125mW·cm-2。The Cu-wrapped polypyrrole nanotube electrocatalyst prepared in this example has a tube diameter of 190 nm, a specific surface area of 820 m 2 /g, and a power density of 125 mW·cm -2 .
实施例8Example 8
一种聚吡咯纳米管电催化剂的制备方法,其特征在于,包括以下步骤:A preparation method of polypyrrole nanotube electrocatalyst, is characterized in that, comprises the following steps:
S1:将NiO分散于水中,搅拌至完全溶解,得到第一溶液;S1: Disperse NiO in water and stir until it is completely dissolved to obtain the first solution;
S2:向第一溶液中加入5mmol/L甲基橙,搅拌至完全溶解,并加入氯化铁,得到第二溶液;S2: Add 5 mmol/L methyl orange to the first solution, stir until completely dissolved, and add ferric chloride to obtain the second solution;
S3:向第二溶液中加入吡咯单体,吡咯单体与氯化铁的物质的量的比例为1:2,吡咯单体与Ni的摩尔比为1:1.5;搅拌发生原位聚合反应后,得到包裹有NiO的聚吡咯纳米管;S3: Add pyrrole monomer to the second solution, the ratio of the amount of pyrrole monomer to ferric chloride is 1:2, and the molar ratio of pyrrole monomer to Ni is 1:1.5; after in-situ polymerization occurs after stirring , to obtain polypyrrole nanotubes wrapped with NiO;
S4:将所述包裹有NiO的聚吡咯纳米管置于氢气气氛中,在600℃下煅烧处理,得到包裹有Ni单质的聚吡咯纳米管电催化剂。S4: placing the NiO-wrapped polypyrrole nanotubes in a hydrogen atmosphere, and calcining them at 600° C. to obtain a Ni simple substance-wrapped polypyrrole nanotube electrocatalyst.
本实施例制得的包裹有Ni单质的聚吡咯纳米管电催化剂的管径为200nm,比表面积为820m2/g,功率密度为135mW·cm-2。The polypyrrole nanotube electrocatalyst coated with simple substance Ni obtained in this example has a diameter of 200 nm, a specific surface area of 820 m 2 /g, and a power density of 135 mW·cm -2 .
实施例9Example 9
一种聚吡咯纳米管电催化剂的制备方法,其特征在于,包括以下步骤:A preparation method of polypyrrole nanotube electrocatalyst, is characterized in that, comprises the following steps:
S1:将Fe2O3分散于水中,搅拌至完全溶解,得到第一溶液;S1: Disperse Fe 2 O 3 in water and stir until completely dissolved to obtain the first solution;
S2:向第一溶液中加入5mmol/L甲基橙,搅拌至完全溶解,并加入氯化铁,得到第二溶液;S2: Add 5 mmol/L methyl orange to the first solution, stir until completely dissolved, and add ferric chloride to obtain the second solution;
S3:向第二溶液中加入吡咯单体,吡咯单体与氯化铁的物质的量的比例为1:2,吡咯单体与Fe2O3中Fe的摩尔比为1:2.5;搅拌发生原位聚合反应后,得到包裹有Fe2O3的聚吡咯纳米管;S3: Add pyrrole monomer to the second solution, the ratio of the amount of pyrrole monomer to ferric chloride is 1:2, and the molar ratio of pyrrole monomer to Fe in Fe2O3 is 1:2.5; stirring occurs After the in-situ polymerization reaction, polypyrrole nanotubes wrapped with Fe 2 O 3 are obtained;
S4:将所述包裹有Fe2O3的聚吡咯纳米管置于氢气气氛中,在600℃下煅烧处理,得到包裹有Fe单质的聚吡咯纳米管电催化剂。S4: placing the polypyrrole nanotubes wrapped with Fe 2 O 3 in a hydrogen atmosphere, and calcining at 600° C. to obtain a polypyrrole nanotube electrocatalyst wrapped with Fe simple substance.
本实施例制得的包裹有Fe单质的聚吡咯纳米管电催化剂的管径为195nm,比表面积为800m2/g,功率密度为150mW·cm-2。The polypyrrole nanotube electrocatalyst coated with Fe simple substance prepared in this example has a tube diameter of 195 nm, a specific surface area of 800 m 2 /g, and a power density of 150 mW·cm -2 .
实施例10Example 10
一种聚吡咯纳米管电催化剂的制备方法,其特征在于,包括以下步骤:A preparation method of polypyrrole nanotube electrocatalyst, is characterized in that, comprises the following steps:
S1:将NiO分散于水中,搅拌至完全溶解,得到第一溶液;S1: Disperse NiO in water and stir until it is completely dissolved to obtain the first solution;
S2:向第一溶液中加入5mmol/L甲基橙,搅拌至完全溶解,并加入氯化铁,得到第二溶液;S2: Add 5 mmol/L methyl orange to the first solution, stir until completely dissolved, and add ferric chloride to obtain the second solution;
S3:向第二溶液中加入吡咯单体,吡咯单体与氯化铁的物质的量的比例为1:2.5,吡咯单体与NiO中Ni的摩尔比为1:2.5;搅拌发生原位聚合反应后,得到包裹有NiO的聚吡咯纳米管;S3: Add pyrrole monomer to the second solution, the ratio of the amount of pyrrole monomer to ferric chloride is 1:2.5, and the molar ratio of pyrrole monomer to Ni in NiO is 1:2.5; stirring in situ polymerization After the reaction, polypyrrole nanotubes wrapped with NiO are obtained;
S4:将所述包裹有NiO的聚吡咯纳米管置于氢气气氛中,在600℃下煅烧处理,得到包裹有Ni单质的聚吡咯纳米管电催化剂。S4: placing the NiO-wrapped polypyrrole nanotubes in a hydrogen atmosphere, and calcining at 600° C. to obtain a Ni simple substance-wrapped polypyrrole nanotube electrocatalyst.
本实施例制得的包裹有Ni单质的聚吡咯纳米管电催化剂的管径为201nm,比表面积为810m2/g,功率密度为155mW·cm-2。The polypyrrole nanotube electrocatalyst coated with Ni simple substance prepared in this example has a tube diameter of 201 nm, a specific surface area of 810 m 2 /g, and a power density of 155 mW·cm -2 .
实施例11Example 11
本实施例与实施例10的区别为加入了NiCl2进行反应。The difference between this embodiment and embodiment 10 is that NiCl was added for reaction.
以上所述仅是本发明的优选实施方式,应当指出,对于本技术领域的普通技术人员来说,在不脱离本发明原理的前提下,还可以作出若干改进和润饰,这些改进和润饰也应视为本发明的保护范围。The above is only a preferred embodiment of the present invention, it should be pointed out that for those of ordinary skill in the art, without departing from the principle of the present invention, some improvements and modifications can also be made, and these improvements and modifications should also be It is regarded as the protection scope of the present invention.
最后所应当说明的是,以上实施例仅用以说明本发明的技术方案而非对本发明保护范围的限制,尽管参照较佳实施例对本发明作了详细说明,本领域的普通技术人员应当理解,可以对本发明的技术方案进行修改或者等同替换,而不脱离本发明技术方案的实质和范围。Finally, it should be noted that the above embodiments are only used to illustrate the technical solutions of the present invention rather than limit the protection scope of the present invention. Although the present invention has been described in detail with reference to the preferred embodiments, those of ordinary skill in the art should understand that The technical solution of the present invention can be modified or equivalently replaced without departing from the spirit and scope of the technical solution of the present invention.
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