CN117174920A - Preparation method and application of a heterostructure ruthenium cobalt boron-based oxide catalyst - Google Patents

Preparation method and application of a heterostructure ruthenium cobalt boron-based oxide catalyst Download PDF

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CN117174920A
CN117174920A CN202310985351.1A CN202310985351A CN117174920A CN 117174920 A CN117174920 A CN 117174920A CN 202310985351 A CN202310985351 A CN 202310985351A CN 117174920 A CN117174920 A CN 117174920A
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cobalt
ruthenium
based oxide
oxide catalyst
boron
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李赛
廖广宁
辛泽怡
李琪
韩锦锦
刘凯
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Xian University of Science and Technology
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Abstract

本发明属于催化剂及其制备技术领域,涉及一种异质结构钌钴硼基氧化物催化剂的制备方法和应用,制备方法包括:1)制备Co‑B前驱体:按照钴元素与硼元素的摩尔比1:2分别称取钴盐和硼氢化物,通过溶解、搅拌、沉淀、分离和干燥,得到Co‑B前驱体;2)制备Ru‑Co‑B基氧化物催化剂:按照钌元素与钴元素的摩尔比1:(4‑16)分别称取钌盐和Co‑B前驱体,经混合研磨、等离子体技术处理,得到Ru‑Co‑B基氧化物催化剂。本发明利用等离子体技术制备异质结构钌钴硼基氧化物催化剂,制备方法简单,易于操作,能大规模制备;且制备的催化剂活性高,用于燃料电池中能提升电池放电性能。

The invention belongs to the technical field of catalysts and their preparation, and relates to a preparation method and application of a heterostructure ruthenium-cobalt-boron-based oxide catalyst. The preparation method includes: 1) Preparing Co-B precursor: According to the molar ratio of cobalt element to boron element Weigh the cobalt salt and borohydride respectively at a ratio of 1:2, and obtain the Co-B precursor through dissolution, stirring, precipitation, separation and drying; 2) Preparation of Ru-Co-B-based oxide catalyst: According to the ruthenium element and cobalt The molar ratio of the elements is 1: (4-16). The ruthenium salt and Co-B precursor are weighed respectively, and after mixing, grinding, and plasma technology treatment, the Ru-Co-B-based oxide catalyst is obtained. The present invention uses plasma technology to prepare a heterostructure ruthenium-cobalt-boron-based oxide catalyst. The preparation method is simple, easy to operate, and can be prepared on a large scale; and the prepared catalyst has high activity, and can improve battery discharge performance when used in fuel cells.

Description

一种异质结构钌钴硼基氧化物催化剂的制备方法和应用Preparation method and application of a heterostructure ruthenium cobalt boron-based oxide catalyst

技术领域Technical field

本发明属于催化剂及其制备技术领域,涉及一种异质结构钌钴硼基氧化物催化剂的制备方法和应用。The invention belongs to the technical field of catalysts and their preparation, and relates to a preparation method and application of a heterostructure ruthenium cobalt boron-based oxide catalyst.

背景技术Background technique

燃料电池是将氢、甲醇、乙醇、碳氢化合物和硼氢化物等燃料的化学能转化为电能的高效清洁电化学发生装置,具有效率高和环境友好等优势。燃料电池被认为是实现能源可持续发展的最有前途的能源转换策略。Fuel cells are efficient and clean electrochemical generating devices that convert the chemical energy of fuels such as hydrogen, methanol, ethanol, hydrocarbons, and borohydrides into electrical energy. They have the advantages of high efficiency and environmental friendliness. Fuel cells are considered the most promising energy conversion strategy to achieve energy sustainability.

目前,燃料电池技术已经有了很大的发展,然而由于大多数催化剂都是由贵金属组成,尤其以Pt金属居多,因贵金属价格昂贵,储量有限等问题,使得燃料电池大规模应用仍然受限。而在低温燃料电池(如质子交换膜燃料电池(PEMFC))、甲醇燃料电池(DMFC)、硼氢化物燃料电池(DBFC))商业化的道路上,燃料电池的持久性和成本是燃料电池能否长远发展并实现商业化的两个主要挑战,所以通过降低电极组件中的贵金属含量,能够直接降低电池成本,但是由于含量的减少,对电池性能和长期稳定性带来影响。At present, fuel cell technology has made great progress. However, because most catalysts are composed of precious metals, especially Pt metal, the large-scale application of fuel cells is still limited due to problems such as expensive precious metals and limited reserves. On the road to commercialization of low-temperature fuel cells (such as proton exchange membrane fuel cells (PEMFC)), methanol fuel cells (DMFC), and borohydride fuel cells (DBFC), the durability and cost of fuel cells are the key to fuel cell energy. There are two main challenges to long-term development and commercialization. Therefore, by reducing the content of precious metals in electrode components, battery costs can be directly reduced. However, due to the reduction in content, battery performance and long-term stability are affected.

近年来,主要通过以下两种途径来降低催化剂成本,提高催化剂的性能:(1)开发研制铂合金催化剂;(2)开发研制非铂电催化剂;虽然上述途径能实现成本和性能方面的优势,但是存在以下问题:目前,对于这类燃料电池催化剂的合成方法,主要是常规化学合成法或高温处理的方式,例如,文献Molten salt assisted to synthesize molybdenumeruthenium boride for hydrogen generation in wide pH range提到采用熔融法,将制备的五氯化钼、氯化钠、氯化钾、无定形硼粉和三氯化钌混合在一起,研磨直到它们变成粉末,然后将上述粉末置于管式炉中,加热后,将获得的纳米材料Mo-Ru-B。文献Ultrafineamorphous Co-W-B alloy as the anode catalyst for a direct borohydride fuelcell采用化学还原法制备了超细非晶态Co-W-B合金。通过用硼氢化钾溶液化学还原氯化钴(CoCl2)和钨酸钠(Na2WO4)合成。将不同体积的CoCl2和Na2WO4溶液混合在一起,以调节样品中的钨含量。然后在磁力搅拌下将KBH4/KOH溶液滴加到混合溶液中,再加入硼氢化钾释放氢气后,搅拌,得到黑色沉淀物过滤并用蒸馏水洗涤,即得到了Co-W-B;专利CN 105702971A介绍了一种燃料电池用核壳型金@钴-硼催化剂。配制钴盐和金盐的混合溶液,将硼氢化物溶于去离子水中配制成硼氢化物溶液,然后向所述硼氢化物溶液中加入氢氧化物,将所述硼氢化物-氢氧化物混合溶液以一定的速度加入钴盐和金盐的混合溶液中,待反应无气体产生后,继续搅拌过滤反应物料得到沉淀,即得到核壳型金@钴-硼催化剂。专利CN201210120922.7介绍了一种燃料电池用碳载核壳型铜钯-铂催化剂及其制备方法。该方法运用了两步还原法,即先还原低活性金属,再还原活性贵金属,通过控制反应的温度和pH值,使贵金属在非贵金属的表面沉积,并辅以脱合金步骤,从而制成核壳型催化剂。In recent years, the following two approaches have been used to reduce catalyst costs and improve catalyst performance: (1) developing platinum alloy catalysts; (2) developing non-platinum electrocatalysts; although the above approaches can achieve advantages in cost and performance, However, there are the following problems: At present, the synthesis method of this type of fuel cell catalyst is mainly conventional chemical synthesis or high-temperature treatment. For example, the literature Molten salt assisted to synthesize molybdenumeruthenium boride for hydrogen generation in wide pH range mentions the use of melting Method, mix the prepared molybdenum pentachloride, sodium chloride, potassium chloride, amorphous boron powder and ruthenium trichloride together, grind them until they become powder, then place the above powder in a tube furnace and heat Finally, the nanomaterial Mo-Ru-B was obtained. Literature Ultrafineamorphous Co-WB alloy as the anode catalyst for a direct borohydride fuel cell uses chemical reduction method to prepare ultrafine amorphous Co-WB alloy. Synthesized by chemical reduction of cobalt chloride (CoCl 2 ) and sodium tungstate (Na 2 WO 4 ) with potassium borohydride solution. Different volumes of CoCl2 and Na2WO4 solutions were mixed together to adjust the tungsten content in the sample. Then add the KBH 4 /KOH solution dropwise into the mixed solution under magnetic stirring, then add potassium borohydride to release hydrogen, stir to obtain a black precipitate, filter it and wash it with distilled water to obtain Co-WB; Patent CN 105702971A introduces A core-shell gold@cobalt-boron catalyst for fuel cells. Prepare a mixed solution of cobalt salt and gold salt, dissolve borohydride in deionized water to prepare a borohydride solution, then add hydroxide to the borohydride solution, and combine the borohydride-hydroxide The mixed solution is added to the mixed solution of cobalt salt and gold salt at a certain speed. After no gas is generated during the reaction, the reaction material is continued to be stirred and filtered to obtain precipitation, thereby obtaining a core-shell gold@cobalt-boron catalyst. Patent CN201210120922.7 introduces a carbon-supported core-shell copper-palladium-platinum catalyst for fuel cells and its preparation method. This method uses a two-step reduction method, that is, first reducing the low-activity metal, and then reducing the active precious metal. By controlling the temperature and pH value of the reaction, the precious metal is deposited on the surface of the non-precious metal, and is supplemented by a dealloying step to form a core. Shell catalyst.

上述的这些方法存在合成过程复杂、能耗高,从长远来看,难以实现大规模生产的问题。The above-mentioned methods have problems such as complex synthesis processes and high energy consumption, which make it difficult to achieve large-scale production in the long run.

发明内容Contents of the invention

为了解决现有燃料电池催化剂存在合成过程复杂的技术问题,本发明提供一种异质结构钌钴硼基氧化物催化剂的制备方法和应用。In order to solve the technical problem of complicated synthesis process of existing fuel cell catalysts, the present invention provides a preparation method and application of a heterostructure ruthenium cobalt boron-based oxide catalyst.

为了实现上述目的,本发明利用等离子体技术制备异质结构钌钴硼基氧化物催化剂,制备方法简单,易于操作,能大规模制备;且制备的催化剂活性高,用于燃料电池中能提升电池放电性能。本发明所用的技术方案具体是:In order to achieve the above purpose, the present invention uses plasma technology to prepare a heterostructure ruthenium cobalt boron-based oxide catalyst. The preparation method is simple, easy to operate, and can be prepared on a large scale; and the prepared catalyst has high activity and can be used in fuel cells to improve battery performance. Discharge performance. The technical solutions used in the present invention are specifically:

一种异质结构钌钴硼基氧化物催化剂的制备方法,其特征在于,包括以下步骤:A method for preparing a heterostructure ruthenium-cobalt-boron-based oxide catalyst, which is characterized by comprising the following steps:

1)制备Co-B前驱体1) Preparation of Co-B precursor

按照钴元素与硼元素的摩尔比1:2分别称取钴盐和硼氢化物,通过溶解、搅拌、沉淀、分离和干燥,得到Co-B前驱体;Weigh the cobalt salt and boron hydride respectively according to the molar ratio of cobalt element to boron element 1:2, and obtain the Co-B precursor through dissolution, stirring, precipitation, separation and drying;

2)制备Ru-Co-B基氧化物催化剂2) Preparation of Ru-Co-B based oxide catalyst

按照钌元素与钴元素的摩尔比1:(4-16)分别称取钌盐和Co-B前驱体,经混合研磨、等离子体技术处理,得到Ru-Co-B催化剂。Weigh the ruthenium salt and Co-B precursor respectively according to the molar ratio of ruthenium element to cobalt element 1: (4-16), and obtain the Ru-Co-B catalyst after mixing, grinding, and plasma technology treatment.

进一步限定,所述步骤2)中,等离子体技术处理的条件为:电压40V-70V,处理时间5min-20min,温度为常温。It is further limited that in step 2), the conditions for plasma technology treatment are: voltage 40V-70V, treatment time 5min-20min, and temperature normal temperature.

进一步限定,所述步骤2)中,钌盐为无水三氯化钌。It is further limited that in step 2), the ruthenium salt is anhydrous ruthenium trichloride.

进一步限定,所述步骤1)具体包括以下步骤:To further limit, said step 1) specifically includes the following steps:

1.1)将称取的钴盐溶解于水中,得到钴盐溶液;1.1) Dissolve the weighed cobalt salt in water to obtain a cobalt salt solution;

1.2)将称取的硼氢化物溶解于水中,得到硼氢化物溶液;1.2) Dissolve the weighed borohydride in water to obtain a borohydride solution;

1.3)将硼氢化物溶液滴加至钴盐溶液中,搅拌至反应完全,经静置沉淀、过滤分离和干燥,得到Co-B前驱体。1.3) Add the borohydride solution dropwise to the cobalt salt solution, stir until the reaction is complete, leave to settle, filter, separate and dry to obtain the Co-B precursor.

进一步限定,所述步骤1.1)中,钴盐为六水合氯化钴,钴盐溶液的浓度为0.015mol/L。It is further limited that in step 1.1), the cobalt salt is cobalt chloride hexahydrate, and the concentration of the cobalt salt solution is 0.015 mol/L.

进一步限定,所述步骤1.2)中,硼氢化物为硼氢化钾,硼氢化钾溶液的浓度为0.03mol/L。It is further limited that in step 1.2), the borohydride is potassium borohydride, and the concentration of the potassium borohydride solution is 0.03 mol/L.

进一步限定,所述步骤1.3)中,滴加速度为1mL/min~2mL/min;干燥条件为:真空度80Pa-100Pa,温度60℃~120℃,时间6h-12h。It is further limited that in the step 1.3), the dropping speed is 1mL/min~2mL/min; the drying conditions are: vacuum degree 80Pa-100Pa, temperature 60℃~120℃, time 6h-12h.

一种异质结构钌钴硼基氧化物催化剂的制备方法所制备的钌钴硼基氧化物催化剂,为核壳-片层镶嵌型异质结构。A method for preparing a heterostructure ruthenium cobalt boron based oxide catalyst. The prepared ruthenium cobalt boron based oxide catalyst is a core-shell-lamellar mosaic type heterostructure.

一种所述的钌钴硼基氧化物催化剂作为阳极催化剂在硼氢化物燃料电池中的应用。An application of the ruthenium cobalt boron-based oxide catalyst as an anode catalyst in a borohydride fuel cell.

进一步限定,所述硼氢化物燃料电池的最大功率密度为143.12mW·cm-2~206.35mW·cm-2It is further limited that the maximum power density of the borohydride fuel cell is 143.12mW·cm -2 ~ 206.35mW·cm -2 .

与现有技术相比,本发明的有益效果是:Compared with the prior art, the beneficial effects of the present invention are:

1、本发明采用等离子技术相结合制备催化剂,与传统的化学合成法相比,方法简单,易于操作,实现大规模生产。1. The present invention uses a combination of plasma technology to prepare the catalyst. Compared with the traditional chemical synthesis method, the method is simple, easy to operate, and can achieve large-scale production.

2、本发明采用低温等离子技术,温度为常温,相比于传统化学法中的高温处理,能耗降低。2. The present invention adopts low-temperature plasma technology and the temperature is normal temperature. Compared with the high-temperature treatment in traditional chemical methods, the energy consumption is reduced.

3、本发明提供的制备方法,首先将反应物充分研磨混合均匀,然后采用低温等离子技术产生高压电场,在高压电场作用下将反应物轰击成离子、原子或是自由基等粒子,使得反应物的结构发生变化,呈现出核壳-片层镶嵌型异质结构,制备的催化剂作为组装在电池中,能极大地提升催化剂的性能,具有优异的电化学性能。3. The preparation method provided by the present invention firstly grinds the reactants thoroughly and mixes them evenly, and then uses low-temperature plasma technology to generate a high-voltage electric field. Under the action of the high-voltage electric field, the reactants are bombarded into particles such as ions, atoms or free radicals, so that the reactants The structure changes and presents a core-shell-lamellar mosaic heterostructure. The prepared catalyst is assembled in a battery, which can greatly improve the performance of the catalyst and has excellent electrochemical performance.

4、本发明制备的钌钴硼基氧化物催化剂,为核壳-片层镶嵌型异质结构,与现有文献报道的球形、核壳结构或中空结构相比,该结构的催化剂成本低、活性高;以碳载氧化铈(CeO2/C)为直接硼氢化物燃料电池DBFC阴极催化剂,Ru-Co-B为阳极催化剂组装的燃料电池,测得燃料电池最大功率密度达到143.12mW·cm-2~206.35mW·cm-2,燃料电池放电性能更优。4. The ruthenium cobalt boron-based oxide catalyst prepared by the present invention is a core-shell-lamellar mosaic heterostructure. Compared with the spherical, core-shell structure or hollow structure reported in the existing literature, the catalyst of this structure has low cost and High activity; the fuel cell assembled with carbon-supported cerium oxide (CeO 2 /C) as the cathode catalyst of the direct borohydride fuel cell DBFC and Ru-Co-B as the anode catalyst, the maximum power density of the fuel cell was measured to reach 143.12mW·cm -2 ~ 206.35mW·cm -2 , the fuel cell discharge performance is better.

4、本发明制备的催化剂以钌、钴、硼组成,且钌元素、钴元素和硼元素的摩尔比为1:(4-16):(8-32),钌元素的摩尔分数为9.09%,贵金属的用量大幅度降低,而当前性格优良的铂基催化剂中铂的含量大概在10%左右,且钌的成本是铂族金属中最低的,价格远远低于铂,使燃料电池成本显著降低,这将有利于促进燃料电池的发展。4. The catalyst prepared by the present invention is composed of ruthenium, cobalt and boron, and the molar ratio of ruthenium element, cobalt element and boron element is 1:(4-16):(8-32), and the molar fraction of ruthenium element is 9.09% , the amount of precious metals used has been greatly reduced, and the platinum content in current platinum-based catalysts with good properties is about 10%, and the cost of ruthenium is the lowest among platinum group metals, and the price is far lower than that of platinum, making the cost of fuel cells significantly higher. This will help promote the development of fuel cells.

附图说明Description of drawings

图1为本发明实施例1制备的Ru-Co-B基氧化物催化剂放大150000倍时的扫描电镜图;Figure 1 is a scanning electron microscope image of the Ru-Co-B-based oxide catalyst prepared in Example 1 of the present invention when magnified 150,000 times;

图2为本发明实施例1制备的Ru-Co-B基氧化物催化剂放大50000倍时的扫描电镜图;Figure 2 is a scanning electron microscope image of the Ru-Co-B-based oxide catalyst prepared in Example 1 of the present invention when magnified 50,000 times;

图3为本发明实施例1制备的Ru-Co-B基氧化物催化剂放大200000倍时的扫描电镜图;Figure 3 is a scanning electron microscope image of the Ru-Co-B-based oxide catalyst prepared in Example 1 of the present invention when magnified 200,000 times;

图4为本发明实施例1制备的Ru-Co-B基氧化物催化剂放大100000倍时的扫描电镜图;Figure 4 is a scanning electron microscope image of the Ru-Co-B-based oxide catalyst prepared in Example 1 of the present invention when magnified 100,000 times;

图5为本发明实施例1制备的Ru-Co-B基氧化物催化剂的EDS谱图;Figure 5 is an EDS spectrum of the Ru-Co-B-based oxide catalyst prepared in Example 1 of the present invention;

图6为本发明实施例1~实施例4制备的Ru-Co-B基氧化物催化剂的XRD谱图;Figure 6 is the XRD spectrum of the Ru-Co-B-based oxide catalyst prepared in Examples 1 to 4 of the present invention;

图7为本发明实施例1制备的Ru-Co-B基氧化物催化剂作直接硼氢化物燃料电池阳极催化剂的功率性能图分别与商业Pt-Ru/C、商业Pt/C、化学法制备的Ru-Co-B和CoB催化剂作直接硼氢化物燃料电池阳极的电池性能对比图;Figure 7 is a power performance diagram of the Ru-Co-B-based oxide catalyst prepared in Example 1 of the present invention as an anode catalyst for a direct borohydride fuel cell, respectively compared with commercial Pt-Ru/C, commercial Pt/C, and chemically prepared Comparison of battery performance of Ru-Co-B and CoB catalysts as anodes of direct borohydride fuel cells;

图8为本发明实施例1制备的Ru-Co-B基氧化物催化剂的恒流放电测试。Figure 8 is a constant current discharge test of the Ru-Co-B-based oxide catalyst prepared in Example 1 of the present invention.

具体实施方式Detailed ways

现结合附图以及实施例对本发明保护的技术方案做详细的说明。The technical solution protected by the present invention will now be described in detail with reference to the accompanying drawings and examples.

一种异质结构钌钴硼基氧化物催化剂的制备方法,包括以下步骤。A method for preparing a heterostructure ruthenium-cobalt-boron-based oxide catalyst, including the following steps.

1)制备Co-B前驱体1) Preparation of Co-B precursor

按照钴元素与硼元素的摩尔比1:2分别称取钴盐和硼氢化物,通过溶解、搅拌、沉淀、分离和干燥,得到Co-B前驱体。Weigh the cobalt salt and boron hydride respectively according to the molar ratio of cobalt element to boron element 1:2, and obtain the Co-B precursor through dissolution, stirring, precipitation, separation and drying.

本步骤Co-B前驱体具体包括以下步骤:The Co-B precursor in this step specifically includes the following steps:

1.1)将称取的钴盐溶解于水中,得到钴盐溶液。1.1) Dissolve the weighed cobalt salt in water to obtain a cobalt salt solution.

优选地,钴盐为六水合氯化钴,但是钴盐还可以使用无水氯化钴、氯化亚钴、硫酸钴、硝酸钴、碳酸钴等,钴盐溶液的浓度为0.015mol/L。Preferably, the cobalt salt is cobalt chloride hexahydrate, but the cobalt salt can also use anhydrous cobalt chloride, cobalt chloride, cobalt sulfate, cobalt nitrate, cobalt carbonate, etc., and the concentration of the cobalt salt solution is 0.015 mol/L.

1.2)将称取的硼氢化物溶解于水中,得到硼氢化物溶液。1.2) Dissolve the weighed borohydride in water to obtain a borohydride solution.

优选地,硼氢化物为硼氢化钾,但是硼氢化物还可以使用硼氢化钠、硼氢化锂等,其中硼氢化物溶液的浓度为0.03mol/L。Preferably, the borohydride is potassium borohydride, but the borohydride can also be sodium borohydride, lithium borohydride, etc., wherein the concentration of the borohydride solution is 0.03 mol/L.

1.3)将硼氢化物溶液滴加至钴盐溶液中,搅拌至反应完全,经静置沉淀、过滤分离和干燥,得到Co-B前驱体。1.3) Add the borohydride solution dropwise to the cobalt salt solution, stir until the reaction is complete, leave to settle, filter, separate and dry to obtain the Co-B precursor.

本步骤中,滴加速度为1mL/min~2mL/min;干燥条件为:真空度80Pa-100Pa,温度60℃~120℃,时间6h-12h。In this step, the dropping speed is 1mL/min~2mL/min; the drying conditions are: vacuum degree 80Pa-100Pa, temperature 60℃~120℃, time 6h-12h.

2)制备Ru-Co-B基氧化物催化剂2) Preparation of Ru-Co-B based oxide catalyst

按照钌元素与钴元素的摩尔比1:(4-16)分别称取钌盐和Co-B前驱体,经混合研磨、等离子体技术处理,得到Ru-Co-B基氧化物催化剂。Weigh the ruthenium salt and Co-B precursor respectively according to the molar ratio of ruthenium element to cobalt element 1: (4-16), and obtain the Ru-Co-B-based oxide catalyst after mixing, grinding, and plasma technology treatment.

具体的,钌盐的摩尔比是按照Co-B前驱体中钴元素与硼元素的摩尔比1:2,制备配置的钴盐物质的量为标准反向推导得出。Specifically, the molar ratio of the ruthenium salt is deduced based on the molar ratio of cobalt element to boron element in the Co-B precursor of 1:2 and the amount of cobalt salt material prepared and configured as a standard.

本步骤中,等离子体技术处理的条件为:电压40V-70V,处理时间5min-20min,温度为常温。In this step, the plasma technology treatment conditions are: voltage 40V-70V, treatment time 5min-20min, and temperature at normal temperature.

优选地,钌盐为无水三氯化钌,但是钌盐也可以选择水溶性三氯化钌(RuCl3·xH2O)、硝酸钌、硫酸钌、醋酸钌等。Preferably, the ruthenium salt is anhydrous ruthenium trichloride, but the ruthenium salt can also be water-soluble ruthenium trichloride (RuCl 3 ·xH 2 O), ruthenium nitrate, ruthenium sulfate, ruthenium acetate, etc.

本发明上述方法制备的钌钴硼基氧化物催化剂为核壳-片层镶嵌型异质结构,能作为阳极催化剂应用于硼氢化物燃料电池中,当以CeO2/C为阴极催化剂,组装的燃料电池的最大功率密度为143.12mW·cm-2~206.35mW·cm-2,放电性能更优。The ruthenium cobalt boron-based oxide catalyst prepared by the above method of the present invention has a core-shell-lamellar mosaic heterostructure and can be used as an anode catalyst in a borohydride fuel cell. When CeO 2 /C is used as a cathode catalyst, the assembled The maximum power density of the fuel cell is 143.12mW·cm -2 ~ 206.35mW·cm -2 , and the discharge performance is better.

下面以几组具体的实施例对本发明的制备方法以及催化剂的性能优势进行阐述。The preparation method of the present invention and the performance advantages of the catalyst are described below with several sets of specific examples.

实施例1Example 1

本实施例中异质结构钌钴硼基氧化物催化剂的制备方法包括以下步骤。The preparation method of the heterostructure ruthenium cobalt boron-based oxide catalyst in this embodiment includes the following steps.

1)制备Co-B前驱体1) Preparation of Co-B precursor

1.1)制备钴盐溶液:称取0.9137g六水合氯化钴,将其溶于去离子水中,定容至250mL容量瓶中,得到浓度为0.015mol/L的六水合氯化钴溶液。1.1) Prepare cobalt salt solution: Weigh 0.9137g cobalt chloride hexahydrate, dissolve it in deionized water, and dilute it to a 250 mL volumetric flask to obtain a cobalt chloride hexahydrate solution with a concentration of 0.015 mol/L.

1.2)制备硼氢化钾溶液:按照钴元素与硼元素的摩尔比为1:2的标准,称取0.4142g硼氢化钾,将硼氢化钾溶于去离子水中,定容至250mL容量瓶中,配制成浓度为0.03mol/L的硼氢化钾溶液。1.2) Prepare potassium borohydride solution: According to the standard that the molar ratio of cobalt element to boron element is 1:2, weigh 0.4142g potassium borohydride, dissolve potassium borohydride in deionized water, and adjust the volume to a 250mL volumetric flask. Prepare a potassium borohydride solution with a concentration of 0.03mol/L.

1.3)制备Co-B前驱体:将0.03mol/L、250mL硼氢化钾溶液缓慢滴入0.015mol/L、250mL的六水合氯化钴溶液中,滴加速度为1mL/min,并不断搅拌,待没有气泡冒出后则反应完全,静置沉淀半小时,然后将其抽滤,并在真空度80Pa、60℃的真空干燥箱中干燥12h,最终得到Co-B前驱体。1.3) Preparation of Co-B precursor: Slowly drop 0.03 mol/L, 250 mL potassium borohydride solution into 0.015 mol/L, 250 mL cobalt chloride hexahydrate solution at a dropping speed of 1 mL/min, and stir continuously until When no bubbles emerge, the reaction is complete. Leave it to settle for half an hour, then filter it and dry it in a vacuum drying oven with a vacuum degree of 80 Pa and 60°C for 12 hours. Finally, the Co-B precursor is obtained.

2)制备Ru-Co-B基氧化物催化剂2) Preparation of Ru-Co-B based oxide catalyst

按照钌元素与钴元素的摩尔比为1:8的标准,称取0.1g无水三氯化钌;将Co-B前驱体按照与无水三氯化钌质量比为1:1的标准,称取0.1g Co-B前驱体,将前驱体与称取的无水三氯化钌混合并充分研磨,然后将混合固体颗粒放入低温等离子体装置中,在空气状态气氛中,电压50V下,通电处理10min,最终得到Ru-Co-B催化剂。According to the standard that the molar ratio of ruthenium element to cobalt element is 1:8, weigh 0.1g anhydrous ruthenium trichloride; according to the standard that the mass ratio of Co-B precursor to anhydrous ruthenium trichloride is 1:1, Weigh 0.1g Co-B precursor, mix the precursor with the weighed anhydrous ruthenium trichloride and grind it thoroughly, then put the mixed solid particles into a low-temperature plasma device, in an air-state atmosphere, at a voltage of 50V , energized for 10 minutes, and finally the Ru-Co-B catalyst was obtained.

本实施例中,低温等离子体装置,其正负电极为不锈钢、铜、铝、铁等导电金属材质。In this embodiment, the positive and negative electrodes of the low-temperature plasma device are made of conductive metal materials such as stainless steel, copper, aluminum, and iron.

对本实施例制备的Ru-Co-B基氧化物催化剂进行性能表征。The performance of the Ru-Co-B-based oxide catalyst prepared in this example was characterized.

1、放大不同倍数下催化剂的SEM扫描图,如图1-图4所示,分别为150000倍、50000倍、200000倍以及100000倍对应的SEM扫描图。1. SEM scans of the catalyst at different magnifications, as shown in Figures 1 to 4, which are the SEM scans corresponding to 150,000 times, 50,000 times, 200,000 times and 100,000 times respectively.

SEM扫描采用的仪器是扫描电镜Hitachi SU8230、在过渡舱中冷场发射且真空状态下进行。The instrument used for SEM scanning is a scanning electron microscope Hitachi SU8230, which is carried out under cold field emission and vacuum conditions in the transition chamber.

从图1~图4中可以看出,按照实施例1合成的Ru-Co-B基氧化物为核壳-片层镶嵌型,且形貌均匀,为纳米级。由此可见,采用等离子体技术制备得到的催化剂是具有异质结构的纳米催化剂,与现有方法制备得到的负载、包裹结构有所不同,结构上发生了较大的变化,由于这种核壳-片层镶嵌型异质结构,使得催化剂的性能得到了大幅度的改善和提高,从而显著优于常规方法制备得到的催化剂。It can be seen from Figures 1 to 4 that the Ru-Co-B-based oxide synthesized according to Example 1 is a core-shell-lamellar mosaic type, and the morphology is uniform and nanoscale. It can be seen that the catalyst prepared by plasma technology is a nanocatalyst with a heterogeneous structure. It is different from the load and wrapping structure prepared by existing methods. The structure has undergone major changes. Due to this core-shell -Layered mosaic heterostructure greatly improves the performance of the catalyst, which is significantly better than catalysts prepared by conventional methods.

2、EDS能谱图2. EDS energy spectrum chart

EDS采用的仪器是美国FEI Talos F200x,在真空状态下,通过电子束的轰击条件下进行测试。The instrument used by EDS is the American FEI Talos F200x, which is tested under vacuum conditions and under electron beam bombardment conditions.

从图5图中可以看出Ru、Co、B三种元素的分布情况,可以得到其三者较好的掺杂在一起。From Figure 5, we can see the distribution of the three elements Ru, Co, and B, and it can be seen that the three elements are well doped together.

3、XRD谱图3. XRD spectrum

XRD采用的仪器是RIGAKU SMARTLAB衍射仪,在扫描角度为10°-80°的范围、扫速为10°/min的扫描条件下进行。The instrument used for XRD is the RIGAKU SMARTLAB diffractometer, which is carried out under the scanning conditions of a scanning angle of 10°-80° and a scanning speed of 10°/min.

从图6中可以得出,不同摩尔比的Ru-Co-B基氧化物的XRD图谱,在2θ=35°左右时,三种元素分别以CoO、RuO2、B20H26O三种物质形成异质结构,且Co、Ru、B三种元素的衍射峰分别与其标准峰(JCPDS NO.42-1300、JCPDS NO.43-1027、JCPDS NO.22-0118)一致,表明通过等离子体作用后成功制备得到Ru-Co-B基氧化物异质结构的催化剂。It can be seen from Figure 6 that the XRD patterns of Ru-Co-B-based oxides with different molar ratios, when 2θ=35°, the three elements are respectively CoO, RuO 2 and B 20 H 26 O A heterogeneous structure is formed, and the diffraction peaks of the three elements Co, Ru, and B are consistent with their standard peaks (JCPDS NO.42-1300, JCPDS NO.43-1027, JCPDS NO.22-0118), indicating that through the plasma Finally, a Ru-Co-B-based oxide heterostructure catalyst was successfully prepared.

4、电池性能4. Battery performance

以本实施例制备的Ru-Co-B基氧化物作为硼氢化物燃料电池DBFC的阳极催化剂,CeO2/C为阴极催化剂组装得到硼氢化物燃料电池,单个DBFC的放电性能通过电池测试系统(来自中国深圳Neware Technology Limited)进行测试,在室温下通入氧气进行测试,测得该燃料电池最大功率密度达到143.12mW·cm-2The Ru-Co-B-based oxide prepared in this example was used as the anode catalyst of the borohydride fuel cell DBFC, and CeO 2 /C was used as the cathode catalyst to assemble a borohydride fuel cell. The discharge performance of a single DBFC was passed by the battery test system ( Neware Technology Limited from Shenzhen, China) conducted tests by introducing oxygen at room temperature, and found that the maximum power density of the fuel cell reached 143.12mW·cm -2 .

实施例2Example 2

本实施例中异质结构钌钴硼基氧化物催化剂的制备方法包括以下步骤。The preparation method of the heterostructure ruthenium cobalt boron-based oxide catalyst in this embodiment includes the following steps.

1)制备Co-B前驱体1) Preparation of Co-B precursor

1.1)制备钴盐溶液:称取0.9137g六水合氯化钴,将其溶于去离子水中,定容至250mL容量瓶中,得到浓度为0.015mol/L的六水合氯化钴溶液。1.1) Prepare cobalt salt solution: Weigh 0.9137g cobalt chloride hexahydrate, dissolve it in deionized water, and dilute it to a 250 mL volumetric flask to obtain a cobalt chloride hexahydrate solution with a concentration of 0.015 mol/L.

1.2)制备硼氢化钾溶液:按照钴元素与硼元素的摩尔比为1:2的标准,称取0.4142g硼氢化钾,将硼氢化钾溶于去离子水中,定容至250mL容量瓶中,配制成浓度为0.03mol/L的硼氢化钾溶液。1.2) Prepare potassium borohydride solution: According to the standard that the molar ratio of cobalt element to boron element is 1:2, weigh 0.4142g potassium borohydride, dissolve potassium borohydride in deionized water, and adjust the volume to a 250mL volumetric flask. Prepare a potassium borohydride solution with a concentration of 0.03mol/L.

1.3)制备Co-B前驱体:将0.03mol/L、250mL硼氢化钾溶液缓慢滴入0.015mol/L、250mL六水合氯化钴溶液中,滴加速度为2mL/min,并不断搅拌,待没有气泡冒出后则反应完全,静置沉淀半小时,然后将其抽滤,并在真空度90Pa、80℃的真空干燥箱中干燥10h,最终得到Co-B前驱体。1.3) Preparation of Co-B precursor: Slowly drop 0.03 mol/L, 250 mL potassium borohydride solution into 0.015 mol/L, 250 mL cobalt chloride hexahydrate solution, with a dropping speed of 2 mL/min, and stir continuously until there is no more When bubbles appear, the reaction is complete. Leave it to settle for half an hour. Then filter it and dry it in a vacuum drying oven with a vacuum of 90 Pa and 80°C for 10 hours. Finally, the Co-B precursor is obtained.

2)制备Ru-Co-B基氧化物催化剂2) Preparation of Ru-Co-B based oxide catalyst

按照钌元素与钴元素的摩尔比为1:9的标准,称取0.0885g无水三氯化钌;将Co-B前驱体按照与无水三氯化钌质量比为1:1的标准,称取0.0885g Co-B前驱体,将前驱体与称取的无水三氯化钌混合并充分研磨,然后将混合固体颗粒放入低温等离子体装置中,在空气状态气氛中,电压50V下,通电处理10min,最终得到Ru-Co-B基氧化物催化剂。According to the standard that the molar ratio of ruthenium element to cobalt element is 1:9, weigh 0.0885g anhydrous ruthenium trichloride; according to the standard that the mass ratio of Co-B precursor to anhydrous ruthenium trichloride is 1:1, Weigh 0.0885g Co-B precursor, mix the precursor with the weighed anhydrous ruthenium trichloride and grind it fully, then put the mixed solid particles into a low-temperature plasma device, in an air-state atmosphere, at a voltage of 50V , energized for 10 minutes, and finally a Ru-Co-B-based oxide catalyst was obtained.

对本实施例制备的Ru-Co-B基氧化物催化剂进行表征。Characterize the Ru-Co-B-based oxide catalyst prepared in this example.

1、XRD谱图1. XRD spectrum

本实例的制备的得到的产物XRD物理表征结果同实例1相同。The XRD physical characterization results of the product prepared in this example are the same as those in Example 1.

2、电池性能2. Battery performance

以本实施例制备的Ru-Co-B基氧化物作为硼氢化物燃料电池DBFC的阳极催化剂,CeO2/C为阴极催化剂组装得到硼氢化物燃料电池,测得该燃料电池最大功率密度达到165.16mW·cm-2The Ru-Co-B-based oxide prepared in this example was used as the anode catalyst of the borohydride fuel cell DBFC, and CeO 2 /C was used as the cathode catalyst to assemble a borohydride fuel cell. It was measured that the maximum power density of the fuel cell reached 165.16 mW·cm -2 .

实施例3Example 3

本实施例中异质结构钌钴硼基氧化物催化剂的制备方法包括以下步骤。The preparation method of the heterostructure ruthenium cobalt boron-based oxide catalyst in this embodiment includes the following steps.

1)制备Co-B前驱体1) Preparation of Co-B precursor

1.1)制备钴盐溶液:称取0.9137g六水合氯化钴,将其溶于去离子水中,定容至250mL容量瓶中,得到浓度为0.015mol/L的六水合氯化钴溶液;1.1) Prepare cobalt salt solution: Weigh 0.9137g cobalt chloride hexahydrate, dissolve it in deionized water, and dilute it to a 250mL volumetric flask to obtain a cobalt chloride hexahydrate solution with a concentration of 0.015 mol/L;

1.2)制备硼氢化钾溶液:按照钴元素与硼元素的摩尔比为1:2的标准,称取0.4142g硼氢化钾,将硼氢化钾溶于去离子水中,定容至250mL容量瓶中,配制成浓度为0.03mol/L的硼氢化钾溶液;1.2) Prepare potassium borohydride solution: According to the standard that the molar ratio of cobalt element to boron element is 1:2, weigh 0.4142g potassium borohydride, dissolve potassium borohydride in deionized water, and adjust the volume to a 250mL volumetric flask. Prepare a potassium borohydride solution with a concentration of 0.03mol/L;

1.3)制备Co-B前驱体:将0.03mol/L、250mL硼氢化钾溶液缓慢滴入0.015mol/L、250mL六水合氯化钴溶液中,滴加速度为1mL/min,并不断搅拌,待没有气泡冒出后则反应完全,静置沉淀半小时,然后将其抽滤,并在真空度100Pa、100℃的真空干燥箱中干燥8h,,最终得到Co-B前驱体;1.3) Preparation of Co-B precursor: Slowly drop 0.03 mol/L, 250 mL potassium borohydride solution into 0.015 mol/L, 250 mL cobalt chloride hexahydrate solution, with a dropping speed of 1 mL/min, and stir continuously until there is no more When bubbles appear, the reaction is complete. Leave it to settle for half an hour. Then filter it and dry it in a vacuum drying oven with a vacuum of 100Pa and 100°C for 8 hours. Finally, the Co-B precursor is obtained;

2)制备Ru-Co-B基氧化物催化剂2) Preparation of Ru-Co-B based oxide catalyst

按照钌元素与钴元素的摩尔比为1:10的标准,称取0.0798g无水三氯化钌;将Co-B前驱体按照与无水三氯化钌质量比为1:1的标准,称取0.0798g Co-B前驱体,将前驱体与称取的无水三氯化钌混合并充分研磨,然后将混合固体颗粒放入低温等离子体装置中,在空气状态气氛中,电压50V下,通电处理10min,最终得到Ru-Co-B基氧化物催化剂。According to the standard that the molar ratio of ruthenium element to cobalt element is 1:10, weigh 0.0798g anhydrous ruthenium trichloride; according to the standard that the mass ratio of Co-B precursor to anhydrous ruthenium trichloride is 1:1, Weigh 0.0798g Co-B precursor, mix the precursor with the weighed anhydrous ruthenium trichloride and grind it fully, then put the mixed solid particles into a low-temperature plasma device, in an air-state atmosphere, at a voltage of 50V , energized for 10 minutes, and finally a Ru-Co-B-based oxide catalyst was obtained.

对本实施例制备的Ru-Co-B基氧化物催化剂进行表征。Characterize the Ru-Co-B-based oxide catalyst prepared in this example.

1、XRD谱图1. XRD spectrum

本实例的制备的得到的产物XRD物理表征结果同实例1相同。The XRD physical characterization results of the product prepared in this example are the same as those in Example 1.

2、电池性能2. Battery performance

以本实施例制备的Ru-Co-B基氧化物作为硼氢化物燃料电池DBFC的阳极催化剂,CeO2/C为阴极催化剂组装得到硼氢化物燃料电池,测得该燃料电池最大功率密度达到206.35mW·cm-2The Ru-Co-B-based oxide prepared in this example was used as the anode catalyst of the borohydride fuel cell DBFC, and CeO 2 /C was used as the cathode catalyst to assemble a borohydride fuel cell. It was measured that the maximum power density of the fuel cell reached 206.35 mW·cm -2 .

实施例4Example 4

本实施例中异质结构钌钴硼催化剂的制备方法包括以下步骤。The preparation method of the heterostructure ruthenium cobalt boron catalyst in this embodiment includes the following steps.

1)制备Co-B前驱体1) Preparation of Co-B precursor

1.1)制备钴盐溶液:称取0.9137g六水合氯化钴,将其溶于去离子水中,定容至250mL容量瓶中,得到浓度为0.015mol/L的六水合氯化钴溶液;1.1) Prepare cobalt salt solution: Weigh 0.9137g cobalt chloride hexahydrate, dissolve it in deionized water, and dilute it to a 250mL volumetric flask to obtain a cobalt chloride hexahydrate solution with a concentration of 0.015 mol/L;

1.2)制备硼氢化钾溶液:按照钴元素与硼元素的摩尔比为1:2的标准,称取0.4142g硼氢化钾,将硼氢化钾溶于去离子水中,定容至250mL容量瓶中,配制成浓度为0.03mol/L的硼氢化钾溶液;1.2) Prepare potassium borohydride solution: According to the standard that the molar ratio of cobalt element to boron element is 1:2, weigh 0.4142g potassium borohydride, dissolve potassium borohydride in deionized water, and adjust the volume to a 250mL volumetric flask. Prepare a potassium borohydride solution with a concentration of 0.03mol/L;

1.3)制备Co-B前驱体:将0.03mol/L、250mL硼氢化钾溶液缓慢滴入0.015mol/L、250mL六水合氯化钴溶液中,滴加速度为2mL/min,并不断搅拌,待没有气泡冒出后则反应完全,静置沉淀半小时,然后将其抽滤,并在真空度100Pa、120℃的真空干燥箱中干燥6h,,最终得到Co-B前驱体。1.3) Preparation of Co-B precursor: Slowly drop 0.03 mol/L, 250 mL potassium borohydride solution into 0.015 mol/L, 250 mL cobalt chloride hexahydrate solution, with a dropping speed of 2 mL/min, and stir continuously until there is no more When bubbles appear, the reaction is complete. Leave it to settle for half an hour. Then filter it and dry it in a vacuum drying oven with a vacuum of 100 Pa and 120°C for 6 hours. Finally, the Co-B precursor is obtained.

2)制备Ru-Co-B基氧化物催化剂2) Preparation of Ru-Co-B based oxide catalyst

按照钌元素与钴元素的摩尔比为1:11的标准,称取0.0724g无水三氯化钌;将Co-B前驱体按照与无水三氯化钌质量比为1:1的标准,称取0.0724g Co-B前驱体,将前驱体与称取的无水三氯化钌混合并充分研磨,然后将混合固体颗粒放入低温等离子体装置中,在空气状态气氛中,电压50V下,通电处理10min,最终得到Ru-Co-B催化剂。According to the standard that the molar ratio of ruthenium element to cobalt element is 1:11, weigh 0.0724g anhydrous ruthenium trichloride; according to the standard that the mass ratio of Co-B precursor to anhydrous ruthenium trichloride is 1:1, Weigh 0.0724g Co-B precursor, mix the precursor with the weighed anhydrous ruthenium trichloride and grind it fully, then put the mixed solid particles into a low-temperature plasma device, in an air-state atmosphere, at a voltage of 50V , energized for 10 minutes, and finally the Ru-Co-B catalyst was obtained.

对本实施例制备的Ru-Co-B基氧化物催化剂进行表征。Characterize the Ru-Co-B-based oxide catalyst prepared in this example.

1、XRD谱图1. XRD spectrum

本实例的制备的得到的产物XRD物理表征结果同实例1相同。The XRD physical characterization results of the product prepared in this example are the same as those in Example 1.

2、电池性能2. Battery performance

以本实施例制备的Ru-Co-B基氧化物作为硼氢化物燃料电池DBFC的阳极催化剂,CeO2/C为阴极催化剂组装得到硼氢化物燃料电池,测得该燃料电池最大功率密度达到170.72mW·cm-2The Ru-Co-B-based oxide prepared in this example was used as the anode catalyst of the borohydride fuel cell DBFC, and CeO 2 /C was used as the cathode catalyst to assemble a borohydride fuel cell. It was measured that the maximum power density of the fuel cell reached 170.72 mW·cm -2 .

综上所述,本发明制备的Ru-Co-B基氧化物作为阳极催化剂用于硼氢化物燃料电池DBFC中,燃料电池最大功率密度达到143.12mW·cm-2~206.35mW·cm-2,催化活性好,放电性能更优。In summary, the Ru-Co-B-based oxide prepared in the present invention is used as an anode catalyst in a borohydride fuel cell DBFC, and the maximum power density of the fuel cell reaches 143.12mW·cm -2 ~ 206.35mW·cm -2 . It has good catalytic activity and better discharge performance.

进一步通过以下实验验证本发明制备的钌钴硼基氧化物催化剂的性能。The performance of the ruthenium cobalt boron-based oxide catalyst prepared in the present invention is further verified through the following experiments.

验证1Verify 1

在同等条件下,将实施例1制备得到的具有异质结构的钌钴硼基氧化物纳米催化剂,与商业Pt/C、商业Pt-Ru/C、化学法制备的钌钴硼催化剂以及钴硼催化剂的功率进行对比,结果参见图7。Under the same conditions, the ruthenium cobalt boron-based oxide nanocatalyst with heterogeneous structure prepared in Example 1 was compared with commercial Pt/C, commercial Pt-Ru/C, chemically prepared ruthenium cobalt boron catalyst and cobalt boron The power of the catalyst is compared, and the results are shown in Figure 7.

化学法制备的钌钴硼催化剂,其操作方法如下:参照实施例1的比例将配置的钌盐溶液、钴盐溶液以及硼化物溶液,三种溶液在常温下依次混合,搅拌均匀即可得到催化剂。The operation method of the ruthenium cobalt boron catalyst prepared by chemical method is as follows: refer to the ratio of Example 1 to mix the three solutions of ruthenium salt solution, cobalt salt solution and boride solution in sequence at room temperature, and stir evenly to obtain the catalyst. .

从图7中可以得出,使用等离子体技术制备得到的具有异质结构的钌钴硼基氧化物纳米催化剂具有优异的电化学性能,其功率远高于其他的催化剂,电池放电性能有所提高。因此,本发明的方法具有良好的应用前景。It can be concluded from Figure 7 that the heterostructured ruthenium-cobalt-boron-based oxide nanocatalyst prepared using plasma technology has excellent electrochemical properties, its power is much higher than other catalysts, and the battery discharge performance has been improved. . Therefore, the method of the present invention has good application prospects.

验证2Verification 2

对实施例1制备的钌钴硼基氧化物催化剂进行稳定性研究。The stability of the ruthenium cobalt boron-based oxide catalyst prepared in Example 1 was studied.

对反复使用一周后的钌钴硼基氧化物催化剂,在恒流放电下,得到电池电压与放电时间的变化趋势,结果如图8所示。For the ruthenium-cobalt-boron-based oxide catalyst after repeated use for a week, under constant current discharge, the changing trend of battery voltage and discharge time was obtained. The results are shown in Figure 8.

参见图8可知,钌钴硼基氧化物催化剂在使用将近一周后,恒流放电下持续八十多个小时,仍然能够具有较好的放电性能,表明该方法制备得到的催化剂稳定性好,具有广阔的商业应用前景。Referring to Figure 8, it can be seen that after nearly a week of use, the ruthenium cobalt boron-based oxide catalyst can still have good discharge performance under constant current discharge for more than 80 hours, indicating that the catalyst prepared by this method has good stability and has Broad commercial application prospects.

以上仅是本发明的几组实施例,并非对本发明作任何限制,凡是根据本发明技术实质对以上实施例所作的任何简单修改、变更以及等效变化,均仍属于本发明技术方案的保护范围内。The above are only a few sets of embodiments of the present invention, and do not limit the present invention in any way. Any simple modifications, changes and equivalent changes made to the above embodiments based on the technical essence of the present invention still belong to the protection scope of the technical solution of the present invention. Inside.

Claims (10)

1.一种异质结构钌钴硼基氧化物催化剂的制备方法,其特征在于,包括以下步骤:1. A method for preparing a heterostructure ruthenium-cobalt-boron-based oxide catalyst, which is characterized by comprising the following steps: 1)制备Co-B前驱体1) Preparation of Co-B precursor 按照钴元素与硼元素的摩尔比1:2分别称取钴盐和硼氢化物,通过溶解、搅拌、沉淀、分离和干燥,得到Co-B前驱体;Weigh the cobalt salt and boron hydride respectively according to the molar ratio of cobalt element to boron element 1:2, and obtain the Co-B precursor through dissolution, stirring, precipitation, separation and drying; 2)制备Ru-Co-B基氧化物催化剂2) Preparation of Ru-Co-B based oxide catalyst 按照钌元素与钴元素的摩尔比1:(4-16)分别称取钌盐和Co-B前驱体,经混合研磨、等离子体技术处理,得到Ru-Co-B基氧化物催化剂。Weigh the ruthenium salt and Co-B precursor respectively according to the molar ratio of ruthenium element to cobalt element 1: (4-16), and obtain the Ru-Co-B-based oxide catalyst after mixing, grinding, and plasma technology treatment. 2.根据权利要求1所述的异质结构钌钴硼基氧化物催化剂的制备方法,其特征在于,所述步骤2)中,等离子体技术处理的条件为:电压40V-70V,处理时间5min-20min,温度为常温。2. The preparation method of the heterostructure ruthenium cobalt boron-based oxide catalyst according to claim 1, characterized in that in step 2), the conditions for plasma technology treatment are: voltage 40V-70V, treatment time 5min -20min, the temperature is normal temperature. 3.根据权利要求1所述的异质结构钌钴硼基氧化物催化剂的制备方法,其特征在于,所述步骤2)中,钌盐为无水三氯化钌、硝酸钌、硫酸钌或醋酸钌。3. The preparation method of the heterostructure ruthenium cobalt boron-based oxide catalyst according to claim 1, characterized in that in step 2), the ruthenium salt is anhydrous ruthenium trichloride, ruthenium nitrate, ruthenium sulfate or Ruthenium acetate. 4.根据权利要求1所述的异质结构钌钴硼基氧化物催化剂的制备方法,其特征在于,所述步骤1)具体包括以下步骤:4. The preparation method of the heterostructure ruthenium cobalt boron-based oxide catalyst according to claim 1, characterized in that the step 1) specifically includes the following steps: 1.1)将称取的钴盐溶解于水中,得到钴盐溶液;1.1) Dissolve the weighed cobalt salt in water to obtain a cobalt salt solution; 1.2)将称取的硼氢化物溶解于水中,得到硼氢化物溶液;1.2) Dissolve the weighed borohydride in water to obtain a borohydride solution; 1.3)将硼氢化物溶液滴加至钴盐溶液中,搅拌至反应完全,经静置沉淀、过滤分离和干燥,得到Co-B前驱体。1.3) Add the borohydride solution dropwise to the cobalt salt solution, stir until the reaction is complete, leave to settle, filter, separate and dry to obtain the Co-B precursor. 5.根据权利要求4所述的异质结构钌钴硼基氧化物催化剂的制备方法,其特征在于,所述步骤1.1)中,钴盐溶液的浓度为0.015mol/L;钴盐为六水合氯化钴、无水氯化钴、氯化亚钴、硫酸钴、硝酸钴或碳酸钴。5. The preparation method of the heterostructure ruthenium cobalt boron-based oxide catalyst according to claim 4, characterized in that in the step 1.1), the concentration of the cobalt salt solution is 0.015 mol/L; the cobalt salt is hexahydrate Cobalt chloride, anhydrous cobalt chloride, cobalt chloride, cobalt sulfate, cobalt nitrate or cobalt carbonate. 6.根据权利要求4所述的异质结构钌钴硼基氧化物催化剂的制备方法,其特征在于,所述步骤1.2)中,硼氢化物为硼氢化钾、硼氢化钠或硼氢化锂,硼氢化钾溶液的浓度为0.03mol/L。6. The preparation method of the heterostructure ruthenium cobalt boron-based oxide catalyst according to claim 4, characterized in that in the step 1.2), the borohydride is potassium borohydride, sodium borohydride or lithium borohydride, The concentration of potassium borohydride solution is 0.03mol/L. 7.根据权利要求4所述的异质结构钌钴硼基氧化物催化剂的制备方法,其特征在于,所述步骤1.3)中,滴加速度为1mL/min~2mL/min;干燥条件为:真空度80Pa-100Pa,温度60℃~120℃,时间6h-12h。7. The preparation method of the heterostructure ruthenium cobalt boron-based oxide catalyst according to claim 4, characterized in that in the step 1.3), the dropping speed is 1mL/min~2mL/min; the drying condition is: vacuum Degree 80Pa-100Pa, temperature 60℃~120℃, time 6h-12h. 8.一种如权利要求1-7任一项所述的异质结构钌钴硼基氧化物催化剂的制备方法所制备的钌钴硼基氧化物催化剂,其特征在于,所述钌钴硼基氧化物催化剂为核壳-片层镶嵌型异质结构。8. A ruthenium cobalt boron based oxide catalyst prepared by the preparation method of a heterostructure ruthenium cobalt boron based oxide catalyst according to any one of claims 1 to 7, characterized in that, the ruthenium cobalt boron based oxide catalyst The oxide catalyst is a core-shell-lamellar mosaic heterostructure. 9.一种如权利要求8所述的钌钴硼基氧化物催化剂作为阳极催化剂在硼氢化物燃料电池中的应用。9. Application of the ruthenium cobalt boron-based oxide catalyst as claimed in claim 8 as an anode catalyst in a borohydride fuel cell. 10.根据权利要求9所述的应用,其特征在于,所述硼氢化物燃料电池的最大功率密度为143.12mW·cm-2~206.35mW·cm-210. The application according to claim 9, characterized in that the maximum power density of the borohydride fuel cell is 143.12mW·cm -2 ~ 206.35mW·cm -2 .
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