CN115928122A - Nickel phosphide electrocatalytic material and preparation method thereof - Google Patents

Nickel phosphide electrocatalytic material and preparation method thereof Download PDF

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CN115928122A
CN115928122A CN202211461217.3A CN202211461217A CN115928122A CN 115928122 A CN115928122 A CN 115928122A CN 202211461217 A CN202211461217 A CN 202211461217A CN 115928122 A CN115928122 A CN 115928122A
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composite material
electrocatalytic
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nickel phosphide
nickel
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CN115928122B (en
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张文涛
周琴
沈家媛
龙剑平
王攀
邓苗
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Chengdu Univeristy of Technology
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Abstract

The invention relates to a nickel phosphide electrocatalytic composite material and a preparation method thereof, belonging to the technical field of electrocatalytic hydrogen production. The invention adopts an in-situ self-growth strategy and prepares nickel phosphide/nickel foam (Ni) with the characteristics of good substrate adhesion, mechanical stability, conductivity and the like by a simple two-step method of in-situ synthesis and low-temperature phosphorization 2 P/NF) electrocatalytic composite material. Under alkaline condition, ni prepared by the invention 2 The P/NF electrocatalytic composite material has the current density of 10 mA/cm 2 The overpotential of the capacitor is only 189mV, and the electric double layer capacitor (C) dl ) The value is as high as 30.68 mF/cm 2 Provides a new material design and synthesis technology for efficiently obtaining clean hydrogen energy.

Description

一种磷化镍电催化材料及其制备方法A kind of nickel phosphide electrocatalytic material and preparation method thereof

技术领域technical field

本发明涉及一种磷化镍电催化复合材料及其制备方法,属于电催化制氢技术领域。The invention relates to a nickel phosphide electrocatalytic composite material and a preparation method thereof, belonging to the technical field of electrocatalytic hydrogen production.

背景技术Background technique

全球化石燃料的大量开发导致了严重的能源危机和环境污染,所以人们对清洁、经济的可持续性能源提出了迫切需求。氢能作为一种取之不竭、来源广泛、高能量密度的清洁能源,可逐步替代石油、天然气等战略性能源商品,能够保障能源安全和多元化,是唯一可以耦合电网、热网和气网的能源,是形成高效、安全、稳定的多能互补能源系统的理想能源品类,在实现“碳达峰、碳中和”目标中将发挥重大作用。电解水制氢因能耗低、整个制备过程中温室气体排放少,制得的氢气纯度高、杂质含量少等特点而备受关注。The massive exploitation of global fossil fuels has led to serious energy crisis and environmental pollution, so people have put forward an urgent demand for clean, economical and sustainable energy. As an inexhaustible clean energy with wide sources and high energy density, hydrogen energy can gradually replace strategic energy commodities such as oil and natural gas, and can ensure energy security and diversification. It is an ideal energy category to form an efficient, safe and stable multi-energy complementary energy system, and will play an important role in realizing the goal of "carbon peaking and carbon neutrality". Hydrogen production by electrolysis of water has attracted much attention due to its low energy consumption, low greenhouse gas emissions during the entire production process, high purity of hydrogen produced, and low impurity content.

目前铂(Pt)系贵金属是性能最佳的析氢反应(HER)电催化剂,但是昂贵的价格和稀缺的资源限制了其大规模应用。因此,制备低成本、高效、稳定的非贵金属催化剂成为目前的研究热点之一。其中,过渡金属化合物(包括过渡金属碳化物、过度金属硫化物、过渡金属氮化物、过渡金属氧化物、过渡金属磷化物和过渡金属硒化物)因独特的物理化学性质、来源广泛、价格低廉等特点而备受关注。但是,大部分金属在电解水制氢过程中,由于吸附氢与金属表面的作用力太强而难以脱附,表现出较差的析氢性能。然而,过渡金属磷化物中,P可以进入金属的晶格中,“稀释”金属原子并维持金属的电子结构基本不变,从而使吸附氢的自由能降低,利于氢的脱附。同时,P的电负性高,能够从金属元素中捕获电子,带负电荷的P也可以作为吸附氢的活性位点,形成的共价键(金属-磷键)也可以提高金属磷化物的稳定性。At present, platinum (Pt)-based noble metals are the best electrocatalysts for hydrogen evolution reaction (HER), but their high price and scarce resources limit their large-scale application. Therefore, the preparation of low-cost, high-efficiency, and stable non-noble metal catalysts has become one of the current research hotspots. Among them, transition metal compounds (including transition metal carbides, transition metal sulfides, transition metal nitrides, transition metal oxides, transition metal phosphides and transition metal selenides) have unique physical and chemical properties, a wide range of sources, and low prices. characteristics have attracted much attention. However, most metals show poor hydrogen evolution performance due to the strong force between the adsorbed hydrogen and the metal surface in the process of hydrogen production by electrolysis of water. However, in transition metal phosphides, P can enter the metal lattice, "dilute" the metal atoms and maintain the electronic structure of the metal basically unchanged, thereby reducing the free energy of hydrogen adsorption and facilitating the desorption of hydrogen. At the same time, P has high electronegativity and can capture electrons from metal elements. Negatively charged P can also be used as an active site for absorbing hydrogen, and the formed covalent bond (metal-phosphorus bond) can also improve the energy efficiency of metal phosphides. stability.

磷化镍因拥有多种不同组分化学式和类似氢化酶的催化机制,国内外学者在此领域开展了诸多研究。如公开号为CN 110512228 A采用化学镀法制备氢氧化镍/含有镍磷镀层的泡沫镍前驱体,然后通过磷化的方式制备了磷化镍/泡沫镍自支撑电极,操作过程复杂,前驱体制备过程中使用原材料多,且需额外添加硫酸镍作为镍源,形成的前驱体与泡沫镍基底粘结力不强,导致制备的磷化镍/泡沫镍自支撑电极稳定性较差。公开号CN113881964 A公开了一种片状磷化镍阵列电极材料的制备方法,首先使用十六烷基三甲基溴化铵和双氧水对泡沫镍进行活化,得到片状氢氧化镍阵列/泡沫镍前驱体,400℃磷化1h得到磷化镍/泡沫镍电极。制备过程中无需添加镍源,但是制备周期长,操作过程复杂,而且需使用表面活性剂。Nickel phosphide has a variety of different component chemical formulas and a catalytic mechanism similar to hydrogenase. Scholars at home and abroad have carried out a lot of research in this field. For example, the publication number is CN 110512228 A, which uses electroless plating to prepare nickel hydroxide/foam nickel precursor containing nickel phosphorus coating, and then prepares nickel phosphide/foam nickel self-supporting electrode by phosphating. The operation process is complicated, and the precursor Many raw materials are used in the preparation process, and nickel sulfate needs to be added as a nickel source. The formed precursor has weak adhesion to the nickel foam substrate, resulting in poor stability of the prepared nickel phosphide/nickel foam self-supporting electrode. Publication No. CN113881964 A discloses a preparation method of sheet-like nickel phosphide array electrode material. First, cetyltrimethylammonium bromide and hydrogen peroxide are used to activate foamed nickel to obtain sheet-shaped nickel hydroxide array/foamed nickel The precursor was phosphated at 400°C for 1 hour to obtain a nickel phosphide/nickel foam electrode. There is no need to add nickel source in the preparation process, but the preparation period is long, the operation process is complicated, and surfactants are required.

针对以上存在的一些问题,通过简单工艺制备一种高效、稳定,绿色经济的电催化复合材料变得尤为重要。In view of some of the above problems, it is particularly important to prepare an efficient, stable, green and economical electrocatalytic composite material through a simple process.

本发明使用的泡沫镍直接为Ni(OH)2的形成提供了镍源,不用添加额外的镍源。因此,所制备的前驱体能够根植于NF中,具有良好的衬底附着性,导电性和机械稳定性,而且低温原位磷化后也依然可以保持住这些特点。The nickel foam used in the present invention directly provides a nickel source for the formation of Ni(OH) 2 without adding an additional nickel source. Therefore, the prepared precursor can be rooted in NF, has good substrate adhesion, electrical conductivity and mechanical stability, and these characteristics can still be maintained after low-temperature in-situ phosphating.

发明内容Contents of the invention

本发明解决的第一个技术问题是提供一种采用自生长策略制备的具有良好基底粘附性、导电性以及机械稳定性的电催化复合材料。The first technical problem solved by the present invention is to provide an electrocatalytic composite material with good substrate adhesion, electrical conductivity and mechanical stability prepared by adopting a self-growth strategy.

本发明解决的第二个技术问题是提供一种电催化复合材料制备方法,包括以下步骤:The second technical problem solved by the present invention is to provide a method for preparing an electrocatalytic composite material, comprising the following steps:

a、取尿素(CO(NH2)2)、氟化铵(NH4F)溶于70mL去离子水中,搅拌均匀得到混合溶液;a. Dissolve urea (CO(NH 2 ) 2 ) and ammonium fluoride (NH 4 F) in 70 mL of deionized water, and stir evenly to obtain a mixed solution;

b、将步骤a中得到的混合溶液与处理过的泡沫镍(NF)片一起转移到聚四氟乙烯内衬的水热釜中,放入烘箱内进行水热反应,待水热结束后冷却至室温,用去离子水和乙醇洗涤,真空干燥得到Ni(OH)2/NF前驱体;b. Transfer the mixed solution obtained in step a together with the processed nickel foam (NF) sheet to a polytetrafluoroethylene-lined hydrothermal kettle, put it into an oven for hydrothermal reaction, and cool it down after the hydrothermal treatment ends to room temperature, washed with deionized water and ethanol, and vacuum-dried to obtain a Ni(OH) 2 /NF precursor;

c、以次亚磷酸钠(NaH2PO2·H2O)为磷源并放置于石英舟尾部,将步骤b中得到的前驱体放置在石英舟顶部,转入氮气气氛的管式炉中加热磷化,降至室温后用去离子水与乙醇洗净,烘干得到Ni2P/NF电催化复合材料。c. Use sodium hypophosphite (NaH 2 PO 2 ·H 2 O) as the phosphorus source and place it at the tail of the quartz boat, place the precursor obtained in step b on the top of the quartz boat, and transfer it to a tube furnace with a nitrogen atmosphere Heating and phosphating, washing with deionized water and ethanol after cooling down to room temperature, and drying to obtain Ni 2 P/NF electrocatalytic composite material.

在一种实施方式中,步骤a中,尿素浓度为5~20mmol/L;优选的,尿素浓度为15mmol/L。In one embodiment, in step a, the urea concentration is 5-20 mmol/L; preferably, the urea concentration is 15 mmol/L.

在一种实施方式中,步骤b中,水热温度为125℃~200℃;优选的,水热温度为150℃。In one embodiment, in step b, the hydrothermal temperature is 125°C to 200°C; preferably, the hydrothermal temperature is 150°C.

在一种实施方式中,步骤b中,水热时间为6~12h;优选的,水热时间量为8h。In one embodiment, in step b, the hydrothermal time is 6-12 hours; preferably, the hydrothermal time is 8 hours.

在一种实施方式中,步骤c中,磷源用量为8:1~16:1;优选的,磷源用量为10:1。In one embodiment, in step c, the amount of phosphorus source is 8:1-16:1; preferably, the amount of phosphorus source is 10:1.

在一种实施方式中,步骤c中,加热升温速率为1℃/min~5℃/min;优选的,升温速率为1℃/min。In one embodiment, in step c, the heating rate is 1° C./min˜5° C./min; preferably, the heating rate is 1° C./min.

在一种实施方式中,步骤c中,加热温度为240℃~300℃;优选的,保温时间为290℃。In one embodiment, in step c, the heating temperature is 240°C-300°C; preferably, the holding time is 290°C.

在一种实施方式中,步骤c中,加热保温时间为1~3h;优选的,保温时间为2h。In one embodiment, in step c, the heating and holding time is 1 to 3 hours; preferably, the holding time is 2 hours.

本发明解决的第三个技术问题是提供了一种所述的电催化复合材料的应用,将其用作高效电解水制氢。The third technical problem solved by the present invention is to provide an application of the electrocatalytic composite material, which is used for high-efficiency electrolysis of water to produce hydrogen.

本发明的有益效果:Beneficial effects of the present invention:

1、本发明所述的电催化复合材料,利用NF本身充当Ni源,氟化铵作为刻蚀剂使NF释放出Ni离子,Ni离子缓慢沉淀,原位反应形成Ni(OH)2前驱体,这种自生长策略,增加了催化剂和导电基底之间的粘附性,有效提高材料的耐用性和稳定性。1. In the electrocatalytic composite material of the present invention, NF itself is used as Ni source, and ammonium fluoride is used as an etchant to release Ni ions from NF, Ni ions slowly precipitate, and react in situ to form Ni(OH) 2 precursors, This self-growth strategy increases the adhesion between the catalyst and the conductive substrate, effectively improving the durability and stability of the material.

2、本发明采用低成本水热法和低温磷化法,制备方法简单,条件温和,原材料来源广泛,成本低。2. The present invention adopts low-cost hydrothermal method and low-temperature phosphating method, the preparation method is simple, the conditions are mild, the source of raw materials is wide, and the cost is low.

附图说明Description of drawings

图1为实施例1所得的Ni2P/NF-8:1电催化复合材料的XRD图。FIG. 1 is the XRD pattern of the Ni 2 P/NF-8:1 electrocatalytic composite material obtained in Example 1.

图2为实施例1所得的Ni2P/NF-8:1电催化复合材料的LSV曲线。Fig. 2 is the LSV curve of the Ni 2 P/NF-8:1 electrocatalytic composite material obtained in Example 1.

图3为实施例1所得的Ni2P/NF-8:1电催化复合材料的Cdl图。Fig. 3 is the C dl diagram of the Ni 2 P/NF-8:1 electrocatalytic composite material obtained in Example 1.

图4为实施例2所得的Ni2P/NF-10:1电催化复合材料的XRD图Fig. 4 is the XRD pattern of Ni 2 P/NF-10:1 electrocatalytic composite material obtained in embodiment 2

图5为实施例2所得的Ni2P/NF-10:1电催化复合材料的LSV曲线。Fig. 5 is the LSV curve of the Ni 2 P/NF-10:1 electrocatalytic composite material obtained in Example 2.

图6为实施例2所得的Ni2P/NF-10:1电催化复合材料的Cdl图。Fig. 6 is the C dl diagram of the Ni 2 P/NF-10:1 electrocatalytic composite material obtained in Example 2.

图7为实施例3所得的Ni2P/NF-12:1电催化复合材料的XRD图。FIG. 7 is the XRD pattern of the Ni 2 P/NF-12:1 electrocatalytic composite material obtained in Example 3.

图8为实施例3所得的Ni2P/NF-12:1电催化复合材料的LSV曲线。Fig. 8 is the LSV curve of the Ni 2 P/NF-12:1 electrocatalytic composite material obtained in Example 3.

图9为实施例1所得的Ni2P/NF-12:1电催化复合材料的Cdl图。FIG. 9 is the C dl diagram of the Ni 2 P/NF-12:1 electrocatalytic composite material obtained in Example 1.

具体实施方式Detailed ways

下面结合实施例对本发明的具体实施方式做进一步的描述,并不因此将本发明限制在所述的实施例范围之中。The specific implementation of the present invention will be further described below in conjunction with the examples, and the present invention is not limited to the scope of the examples.

电催化测试Electrocatalytic test

电催化析氢反应测试在浓度为1M KOH溶液中进行,Ni2P/NF复合材料的大小为1*1cm,以碳棒为对电极,Hg/HgO为参比电极,以玻碳电极夹夹住Ni2P/NF复合材料为工作电极,电化学性能测试在电化学工作站DH7000(东华测试)上进行。The electrocatalytic hydrogen evolution reaction test was carried out in a KOH solution with a concentration of 1M. The size of the Ni 2 P/NF composite material was 1*1cm, with a carbon rod as the counter electrode, Hg/HgO as the reference electrode, and a glassy carbon electrode clamp. The Ni 2 P/NF composite material was used as the working electrode, and the electrochemical performance test was carried out on an electrochemical workstation DH7000 (Donghua Test).

实施例1Example 1

合成过程:Synthesis:

a、取0.047g尿素(CO(NH2)2)、0.023g氟化铵(NH4F)溶于70mL去离子水中,搅拌均匀得到混合溶液;a. Dissolve 0.047g of urea (CO(NH 2 ) 2 ) and 0.023g of ammonium fluoride (NH 4 F) in 70mL of deionized water, and stir evenly to obtain a mixed solution;

b、将步骤a中得到的混合溶液与处理过的泡沫镍(NF)片一起转移到聚四氟乙烯内衬的水热釜中,放入烘箱内125℃保温6h,待水热结束后冷却至室温,用去离子水和乙醇洗涤,60℃真空干燥得到Ni(OH)2/NF前驱体;b. Transfer the mixed solution obtained in step a together with the processed nickel foam (NF) sheet to a polytetrafluoroethylene-lined hydrothermal kettle, put it in an oven at 125°C for 6 hours, and cool it down after the hydrothermal treatment ends to room temperature, washed with deionized water and ethanol, and vacuum-dried at 60°C to obtain a Ni(OH) 2 /NF precursor;

c、以质量比为8:1的次亚磷酸钠(NaH2PO2·H2O)为磷源并放置于石英舟尾部,将步骤b中得到的前驱体放置在石英舟顶部,转入氮气氛的管式炉中以2℃/min升温至300℃磷化1h,降至室温后用去离子水与乙醇洗净,烘干得到Ni2P/NF-8:1电催化复合材料。c. Use sodium hypophosphite (NaH 2 PO 2 ·H 2 O) with a mass ratio of 8:1 as the phosphorus source and place it at the tail of the quartz boat, place the precursor obtained in step b on the top of the quartz boat, and transfer to In a tube furnace in a nitrogen atmosphere, the temperature was raised to 300 °C for 1 h at 2 °C/min, and after cooling down to room temperature, it was washed with deionized water and ethanol, and dried to obtain a Ni 2 P/NF-8:1 electrocatalytic composite material.

图1为本发明实施例1所得的Ni2P/NF-8:1电催化复合材料的XRD图,由图1可知,实施例1所制得的Ni2P/NF-8:1的XRD结果与标准衍射峰相符,并无其他杂质,证明了磷化的成功性。Fig. 1 is the XRD pattern of Ni 2 P/NF-8:1 electrocatalytic composite material obtained in Example 1 of the present invention, as can be seen from Fig. 1, the XRD of Ni 2 P/NF-8:1 prepared in Example 1 The results are consistent with the standard diffraction peaks, and there are no other impurities, which proves the success of phosphating.

图2为本发明实施例1所得的Ni2P/NF-8:1电催化复合材料的LSV图,由图2可知,实施例1所得的Ni2P/NF-8:1电催化复合材料在电流密度为10mA cm-2时的过电位为263mV。Fig. 2 is the LSV diagram of the Ni 2 P/NF-8:1 electrocatalytic composite material obtained in Example 1 of the present invention, as can be seen from Fig. 2, the Ni 2 P/NF-8:1 electrocatalytic composite material obtained in Example 1 The overpotential is 263mV when the current density is 10mA cm -2 .

图3为本发明实施例1所得的Ni2P/NF-8:1电催化复合材料的Cdl值,由图3可知,实施例1所制得的Ni2P/NF-8:1的Cdl值为14.83mF/cm2Fig. 3 is the C dl value of Ni 2 P/NF-8:1 electrocatalytic composite material obtained in Example 1 of the present invention, as can be seen from Fig. 3, the Ni 2 P/NF-8:1 that embodiment 1 makes The C dl value is 14.83 mF/cm 2 .

实施例2Example 2

合成过程:Synthesis:

a、取0.063g尿素(CO(NH2)2)、0.023g氟化铵(NH4F)溶于70mL去离子水中,搅拌均匀得到混合溶液;a. Dissolve 0.063g of urea (CO(NH 2 ) 2 ) and 0.023g of ammonium fluoride (NH 4 F) in 70mL of deionized water, and stir evenly to obtain a mixed solution;

b、将步骤a中得到的混合溶液与处理过的泡沫镍(NF)片一起转移到聚四氟乙烯内衬的水热釜中,放入烘箱内150℃保温8h,待水热结束后冷却至室温,用去离子水和乙醇洗涤,60℃真空干燥得到Ni(OH)2/NF前驱体;b. Transfer the mixed solution obtained in step a together with the processed nickel foam (NF) sheet to a polytetrafluoroethylene-lined hydrothermal kettle, put it in an oven at 150°C for 8 hours, and cool it after the hydrothermal treatment ends to room temperature, washed with deionized water and ethanol, and vacuum-dried at 60°C to obtain a Ni(OH) 2 /NF precursor;

c、以质量比为10:1的次亚磷酸钠(NaH2PO2·H2O)为磷源并放置于石英舟尾部,将步骤b中得到的前驱体放置在石英舟顶部,转入氮气氛的管式炉中以1℃/min升温至290℃磷化2h,降至室温后用去离子水与乙醇洗净,烘干得到Ni2P/NF-10:1电催化复合材料。c. Use sodium hypophosphite (NaH 2 PO 2 ·H 2 O) with a mass ratio of 10:1 as the phosphorus source and place it at the tail of the quartz boat, place the precursor obtained in step b on the top of the quartz boat, and transfer to In a tube furnace in a nitrogen atmosphere, the temperature was raised to 290 °C for 2 h at 1 °C/min, and after cooling down to room temperature, it was washed with deionized water and ethanol, and dried to obtain a Ni 2 P/NF-10:1 electrocatalytic composite material.

图4为本发明实施例2所得的Ni2P/NF-10:1电催化复合材料的XRD图,由图4可知,实施例2所制得的Ni2P/NF-10:1的XRD结果与标准衍射峰相符,并无其他杂质,证明了磷化的成功性。Fig. 4 is the XRD pattern of Ni 2 P/NF-10:1 electrocatalytic composite material obtained in Example 2 of the present invention, as can be seen from Fig. 4, the XRD of Ni 2 P/NF-10:1 prepared in Example 2 The results are consistent with the standard diffraction peaks, and there are no other impurities, which proves the success of phosphating.

图5为本发明实施例2所得的Ni2P/NF-10:1电催化复合材料的LSV图,由图5可知,实施例2所得的Ni2P/NF-10:1电催化复合材料在电流密度为10mA cm-2时的过电位为189mV。Fig. 5 is the LSV diagram of the Ni 2 P/NF-10:1 electrocatalytic composite material obtained in Example 2 of the present invention, as can be seen from Fig. 5, the Ni 2 P/NF-10:1 electrocatalytic composite material obtained in Example 2 The overpotential is 189mV at a current density of 10mA cm -2 .

图6为本发明实施例2所得的Ni2P/NF-10:1电催化复合材料的Cdl值,由图6可知,实施例2所制得的Ni2P/NF-10:1的Cdl值为30.18mF/cm2Fig. 6 is the C dl value of the Ni 2 P/NF-10:1 electrocatalytic composite material obtained in Example 2 of the present invention, as can be seen from Fig. 6, the Ni 2 P/NF-10:1 that the embodiment 2 makes The C dl value is 30.18 mF/cm 2 .

实施例3Example 3

合成过程:Synthesis:

a、取0.084g尿素(CO(NH2)2)、0.023g氟化铵(NH4F)溶于70mL去离子水中,搅拌均匀得到混合溶液;a. Dissolve 0.084g of urea (CO(NH 2 ) 2 ) and 0.023g of ammonium fluoride (NH 4 F) in 70mL of deionized water, and stir evenly to obtain a mixed solution;

b、将步骤a中得到的混合溶液与处理过的泡沫镍(NF)片一起转移到聚四氟乙烯内衬的水热釜中,放入烘箱内175℃保温10h,待水热结束后冷却至室温,用去离子水和乙醇洗涤,60℃真空干燥得到Ni(OH)2/NF前驱体;b. Transfer the mixed solution obtained in step a together with the processed nickel foam (NF) sheet to a polytetrafluoroethylene-lined hydrothermal kettle, put it in an oven at 175°C and keep it warm for 10h, and cool it down after the hydrothermal treatment ends to room temperature, washed with deionized water and ethanol, and vacuum-dried at 60°C to obtain a Ni(OH) 2 /NF precursor;

c、以质量比为12:1的次亚磷酸钠(NaH2PO2·H2O)为磷源并放置于石英舟尾部,将步骤b中得到的前驱体放置在石英舟顶部,转入氮气氛的管式炉中以5℃/min升温至280℃磷化3h,降至室温后用去离子水与乙醇洗净,烘干得到Ni2P/NF-12:1电催化复合材料。c. Use sodium hypophosphite (NaH 2 PO 2 ·H 2 O) with a mass ratio of 12:1 as the phosphorus source and place it at the tail of the quartz boat, place the precursor obtained in step b on the top of the quartz boat, and transfer to In a nitrogen atmosphere tube furnace, the temperature was raised to 280°C for 3h at 5°C/min, and after cooling down to room temperature, it was washed with deionized water and ethanol, and dried to obtain Ni 2 P/NF-12:1 electrocatalytic composite material.

图7为本发明实施例3所得的Ni2P/NF-12:1电催化复合材料的XRD图,由图7可知,实施例3所制得的Ni2P/NF-12:1的XRD结果与标准衍射峰相符,并无其他杂质,证明了磷化的成功性。Fig. 7 is the XRD pattern of the Ni 2 P/NF-12:1 electrocatalytic composite material obtained in Example 3 of the present invention, as can be seen from Fig. 7, the XRD of Ni 2 P/NF-12:1 prepared in Example 3 The results are consistent with the standard diffraction peaks, and there are no other impurities, which proves the success of phosphating.

图8为本发明实施例3所得的Ni2P/NF-12:1电催化复合材料的LSV图,由图8可知,实施例3所得的Ni2P/NF-12:1电催化复合材料在电流密度为10mA cm-2时的过电位为216mV。Fig. 8 is the LSV diagram of the Ni2P/NF-12:1 electrocatalytic composite material obtained in Example 3 of the present invention, as can be seen from Fig. 8, the Ni2P /NF-12:1 electrocatalytic composite material obtained in Example 3 is The overpotential at a density of 10mA cm -2 is 216mV.

图9为本发明实施例3所得的Ni2P/NF-12:1电催化复合材料的Cdl值,由图9可知,实施例3所制得的Ni2P/NF-12:1的Cdl值为19.33mF/cm2Fig. 9 is the C dl value of Ni 2 P/NF-12:1 electrocatalytic composite material obtained in Example 3 of the present invention, as can be seen from Fig. 9, Ni 2 P/NF-12:1 prepared in Example 3 The C dl value is 19.33 mF/cm 2 .

Claims (10)

1. A nickel phosphide electrocatalytic composite material and a preparation method thereof are characterized in that: the invention adopts a self-growth strategy and prepares nickel phosphide/nickel foam (Ni) with the characteristics of good substrate adhesion, mechanical stability, conductivity and the like by a simple two-step method of in-situ synthesis and low-temperature phosphorization 2 P/NF) electrocatalytic composite material to realize excellent hydrogen production performance by electrocatalytic decomposition of water.
2. The nickel phosphide electrocatalytic composite material as set forth in claim 1 and the preparation method thereof, characterized by comprising the steps of:
a. taking urea (CO (NH) 2 ) 2 ) Ammonium fluoride (NH) 4 F) Dissolving in 70mL of deionized water, and uniformly stirring to obtain a mixed solution;
b. mixing the mixed solution obtained in the step a with treated foam Nickel (NF)) Transferring the slices into a hydrothermal kettle with a polytetrafluoroethylene lining, putting the hydrothermal kettle into an oven for hydrothermal reaction, cooling to room temperature after hydrothermal reaction, washing with deionized water and ethanol, and vacuum drying to obtain Ni (OH) 2 a/NF precursor;
c. with sodium hypophosphite (NaH) 2 PO 2 ·H 2 O) is used as a phosphorus source and is placed at the tail part of the quartz boat, the precursor obtained in the step b is placed at the top of the quartz boat, the quartz boat is transferred into a tube furnace with nitrogen atmosphere for heating and phosphorization, the temperature is reduced to room temperature, then deionized water and ethanol are used for cleaning, and drying is carried out to obtain Ni 2 P/NF electrocatalytic composite material.
3. The nickel phosphide electrocatalytic composite material and the preparation method thereof as claimed in claim 2, wherein: in the step a, the concentration of the urea is 5-20 mmol/L.
4. The nickel phosphide electrocatalytic composite material and the preparation method thereof as claimed in claim 2, wherein: in the step b, the hydrothermal temperature is 125-200 ℃.
5. The nickel phosphide electrocatalytic composite material and the preparation method thereof as claimed in claim 2, wherein: in the step b, the hydrothermal time is 6-12 h.
6. The nickel phosphide electrocatalytic composite material and the preparation method thereof as claimed in claim 2, wherein the nickel phosphide electrocatalytic composite material comprises the following components in percentage by weight: in the step c, the dosage of the phosphorus source is 8:1-16 by mass ratio.
7. The nickel phosphide electrocatalytic composite material and the preparation method thereof as claimed in claim 2, wherein: in the step c, the heating rate is 1-5 ℃/min.
8. The nickel phosphide electrocatalytic composite material and the preparation method thereof as claimed in claim 2, wherein: in the step c, the heating temperature is 240-300 ℃.
9. The nickel phosphide electrocatalytic composite material and the preparation method thereof as claimed in claim 2, wherein: in the step c, the heating and heat preservation time is 1-3 h.
10. Use of a nickel phosphide electrocatalytic composite material as set forth in claim 1 or prepared by the preparation method as set forth in any one of claims 2 to 8 as an electrocatalytic water decomposition catalyst.
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