CN111644168A - Method for preparing atomic-scale catalyst by slowly raising temperature to greatly improve yield of hydrogen peroxide - Google Patents
Method for preparing atomic-scale catalyst by slowly raising temperature to greatly improve yield of hydrogen peroxide Download PDFInfo
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Abstract
本发明涉及一种缓慢升温制备原子级催化剂以大幅提升过氧化氢产量的方法,属于材料科学与工程技术和化学领域。本发明制备的催化剂原料为酞菁金属与碳纳米材料,涉及的金属有Fe、Co、Ni、Mn、Cu、Zn等非贵金属元素。首先配置含一定负载比例的酞菁金属与前驱体氟化碳纳米管混合液A,常温下进行超声、搅拌,使其充分反应并负载均匀,待负载完成后去除分散溶剂,把制备好的中间产物B放入管式炉中,惰性气体条件下加热数小时,得到产物C。本方法具有操作简单、效率高、应用范围广等优点。相对于传统制备过氧化氢的方法具有易操作、产量高、安全可靠等优势。
The invention relates to a method for slowly heating up an atomic-level catalyst to greatly increase the yield of hydrogen peroxide, and belongs to the fields of material science and engineering technology and chemistry. The catalyst raw materials prepared by the invention are metal phthalocyanine and carbon nanomaterials, and the involved metals include non-precious metal elements such as Fe, Co, Ni, Mn, Cu, and Zn. First, configure the mixed solution A of metal phthalocyanine and precursor fluorinated carbon nanotubes containing a certain loading ratio, ultrasonically and stir at room temperature to make it fully react and load evenly. After the loading is completed, remove the dispersing solvent, and put the prepared intermediate Product B was placed in a tube furnace and heated under inert gas conditions for several hours to obtain product C. The method has the advantages of simple operation, high efficiency and wide application range. Compared with the traditional method for preparing hydrogen peroxide, it has the advantages of easy operation, high yield, safety and reliability.
Description
技术领域technical field
本发明涉及一种缓慢升温制备原子级催化剂以大幅提升过氧化氢产量的方法,属于材料科学与工程技术和化学领域。The invention relates to a method for slowly heating up an atomic-level catalyst to greatly increase the yield of hydrogen peroxide, and belongs to the fields of material science and engineering technology and chemistry.
背景技术Background technique
过氧化氢不仅是一种用途广泛且对环境无害的化学氧化剂,广泛用于水处理、纸浆漂白和化学合成,而且是一种潜在的储能物质。如今,对过氧化氢的大量需求使这种化学品成为世界上重要的产品之一。然而,过氧化氢的工业生产主要基于在近70年前发展起来的Riedl-Pfleidererpro(里德尔·普夫莱德里埃普罗)过程,涉及蒽醌的顺序加氢和氧化。这一过程的固有复杂性和高能耗促进了研究人员探索过氧化氢生产的替代工艺。在此背景下,开发一种在碱性介质中将O2部分还原为H2O2的电化学过程将是一种有吸引力的策略,然而,目前我们仍然缺乏能在过氧化氢的生产中,表现出高活性和选择性、实用和成本效益高的电催化剂。考虑到温度作为影响化学反应动力学和热力学的重要参数,本方法采用一种广泛应用的催化剂制备法,缓慢升温法,控制气体环境下提高温度,改变物质元素间成键方式,激活金属的催化位点,在适宜热激活温度下,使得金属原子与NFC结合形成高效活性中心,得到一种具有较强ORR性能的催化剂。该催化剂在两电子和四电子O2还原途径中,具有更强的HOO*的吸附能力,达到较高的过氧化氢催化活性,大幅度提升了电化学催化中过氧化氢的产率。Hydrogen peroxide is not only a versatile and environmentally friendly chemical oxidant widely used in water treatment, pulp bleaching and chemical synthesis, but also a potential energy storage substance. Today, the high demand for hydrogen peroxide makes this chemical one of the most important products in the world. However, the industrial production of hydrogen peroxide is mainly based on the Riedl-Pfleidererpro process developed nearly 70 years ago, involving the sequential hydrogenation and oxidation of anthraquinones. The inherent complexity and high energy consumption of this process has prompted researchers to explore alternative processes for hydrogen peroxide production. In this context, it would be an attractive strategy to develop an electrochemical process for the partial reduction of O2 to H2O2 in an alkaline medium, however, we still lack the ability to produce hydrogen peroxide in an alkaline medium. , exhibit high activity and selectivity, practical and cost-effective electrocatalysts. Considering that temperature is an important parameter affecting the kinetics and thermodynamics of chemical reactions, this method adopts a widely used catalyst preparation method, slow heating method, increasing the temperature under controlled gas environment, changing the bonding method between material elements, and activating the catalysis of metals. At a suitable thermal activation temperature, the metal atoms are combined with NFC to form an efficient active center, and a catalyst with strong ORR performance is obtained. The catalyst has stronger adsorption capacity of HOO* in the two-electron and four-electron O 2 reduction pathways, achieves high hydrogen peroxide catalytic activity, and greatly improves the yield of hydrogen peroxide in electrochemical catalysis.
发明内容SUMMARY OF THE INVENTION
1、本发明的目标1. Object of the present invention
本发明的目的是得到一种大幅提升过氧化氢产量的方法。通过缓慢升温法就可以提升金属催化剂的ORR性能及极高的过氧化氢选择性。The purpose of the present invention is to obtain a kind of method that greatly improves the hydrogen peroxide production. The ORR performance and extremely high hydrogen peroxide selectivity of the metal catalyst can be improved by the slow heating method.
2、本技术的发明要点2. The main points of the invention of this technology
本发明要点如下:The main points of the present invention are as follows:
(1)用酞菁金属、无机材料和溶剂配置成质量-体积浓度为2-4mg/ml的反应物溶液A,所述的金属盐元素为Fe、Co、Ni、Mn、Cu、Zn,所述的无机材料为氟化碳纳米管,所述的溶剂为无水乙醇。(1) A reactant solution A with a mass-volume concentration of 2-4 mg/ml is prepared with metal phthalocyanine, inorganic materials and a solvent, and the metal salt elements are Fe, Co, Ni, Mn, Cu, and Zn, so The inorganic material is fluorinated carbon nanotubes, and the solvent is anhydrous ethanol.
(2)将溶液超声至无颗粒存在后,搅拌12小时,抽滤,在定性滤纸上得到反应物。待反应物干燥完全,将得到的反应物放在真空管式炉中煅烧,一般使用氮气或氩气作为保护气体,退火温度为500℃~800℃,退火时间为9-14h,保温时间为1h,升温速率为1℃/min(2) After sonicating the solution until no particles exist, stirring for 12 hours, suction filtration, and obtaining the reactant on qualitative filter paper. After the reactants are completely dried, the obtained reactants are calcined in a vacuum tube furnace, generally using nitrogen or argon as the protective gas, the annealing temperature is 500℃~800℃, the annealing time is 9-14h, and the holding time is 1h. The heating rate is 1°C/min
本发明提出的缓慢升温制备催化剂提升高过氧化氢产率,其优点是:这种方法适用范围广泛,可以合成多种金属催化剂,如Fe、Co、Ni、Mn、Cu、Zn等,且化学性能稳定,原材料易获取,合成工艺简单,可以大规模生产。The slow heating-up preparation catalyst proposed by the present invention improves the high hydrogen peroxide yield, and the advantages are: this method has a wide range of applications, and can synthesize various metal catalysts, such as Fe, Co, Ni, Mn, Cu, Zn, etc., and the chemical The performance is stable, the raw materials are easily obtained, the synthesis process is simple, and it can be mass-produced.
附图说明Description of drawings
图1是本发明方法负载酞菁钴后纳米管的扫描透射电子显微镜图。图2是掺钴元素催化剂催化下过氧化氢产量与电子转移数对比图;FIG. 1 is a scanning transmission electron microscope image of the nanotubes loaded with cobalt phthalocyanine according to the method of the present invention. Figure 2 is a comparison diagram of hydrogen peroxide yield and electron transfer number under the catalysis of cobalt-doped catalyst;
具体实施方式Detailed ways
以下介绍本发明方法的实施例:Embodiments of the inventive method are introduced below:
实施例1Example 1
3%-800℃-Co-NFC催化剂的制备Preparation of 3%-800℃-Co-NFC catalyst
首先,把酞菁钴、氟化碳纳米管和无水乙醇充分混合,酞菁钴与前驱体的负载量比例为 3%,配置成2mg/ml的混合溶液A,将溶液超声至无颗粒存在后,搅拌12小时,抽滤,在定性滤纸上得到反应物。待反应物干燥完全,将得到的反应物放在真空管式炉中煅烧,一般使用氮气或氩气作为保护气体,退火温度为800℃,保温时间为1h,升温速率为1℃/min,待加热完毕后,冷却至室温,得到最后的产物。First, mix cobalt phthalocyanine, fluorinated carbon nanotubes and anhydrous ethanol thoroughly. The loading ratio of cobalt phthalocyanine to the precursor is 3%, and configure a mixed solution A of 2 mg/ml. The solution is sonicated until no particles exist. After that, it was stirred for 12 hours, filtered with suction, and the reactant was obtained on qualitative filter paper. After the reactants are completely dried, the obtained reactants are calcined in a vacuum tube furnace. Generally, nitrogen or argon is used as a protective gas. The annealing temperature is 800°C, the holding time is 1h, and the heating rate is 1°C/min. After completion, cooling to room temperature yielded the final product.
实施例2Example 2
3%-800℃-Fe-NFC催化剂的制备Preparation of 3%-800℃-Fe-NFC catalyst
首先,把酞菁铁、氟化碳纳米管和无水乙醇充分混合,酞菁铁与前驱体的负载量比例为 3%,配置成2mg/ml的混合溶液A,将溶液超声至无颗粒存在后,搅拌12小时,抽滤,在定性滤纸上得到反应物。待反应物干燥完全,将得到的反应物放在真空管式炉中煅烧,一般使用氮气或氩气作为保护气体,退火温度为800℃,保温时间为1h,升温速率为1℃/min,待加热完毕后,冷却至室温,得到最后的产物。First, fully mix iron phthalocyanine, fluorinated carbon nanotubes and anhydrous ethanol, the loading ratio of iron phthalocyanine to precursor is 3%, configure a mixed solution A of 2 mg/ml, and sonicate the solution until no particles exist. After that, it was stirred for 12 hours, filtered with suction, and the reactant was obtained on qualitative filter paper. After the reactants are completely dried, the obtained reactants are calcined in a vacuum tube furnace. Generally, nitrogen or argon is used as a protective gas. The annealing temperature is 800°C, the holding time is 1h, and the heating rate is 1°C/min. After completion, cooling to room temperature yielded the final product.
实施例3Example 3
3%-800℃-Cu-NFC催化剂的制备Preparation of 3%-800℃-Cu-NFC catalyst
首先,把酞菁铜、氟化碳纳米管和无水乙醇充分混合,酞菁铜与前驱体的负载量比例为 3%,配置成2mg/ml的混合溶液A,将溶液超声至无颗粒存在后,搅拌12小时,抽滤,在定性滤纸上得到反应物。待反应物干燥完全,将得到的反应物放在真空管式炉中煅烧,一般使用氮气或氩气作为保护气体,退火温度为800℃,保温时间为1h,升温速率为1℃/min,待加热完毕后,冷却至室温,得到最后的产物。First, fully mix copper phthalocyanine, carbon fluoride nanotubes and absolute ethanol, the loading ratio of copper phthalocyanine to precursor is 3%, configure a mixed solution A of 2 mg/ml, and sonicate the solution until no particles exist After that, it was stirred for 12 hours, filtered with suction, and the reactant was obtained on qualitative filter paper. After the reactants are completely dried, the obtained reactants are calcined in a vacuum tube furnace. Generally, nitrogen or argon is used as a protective gas. The annealing temperature is 800°C, the holding time is 1h, and the heating rate is 1°C/min. After completion, cooling to room temperature yielded the final product.
实施例4Example 4
3%-800℃-Ni-NFC催化剂的制备Preparation of 3%-800℃-Ni-NFC catalyst
首先,把酞菁镍、氟化碳纳米管和无水乙醇充分混合,酞菁镍与前驱体的负载量比例为 3%,配置成2mg/ml的混合溶液A,将溶液超声至无颗粒存在后,搅拌12小时,抽滤,在定性滤纸上得到反应物。待反应物干燥完全,将得到的反应物放在真空管式炉中煅烧,一般使用氮气或氩气作为保护气体,退火温度为800℃,保温时间为1h,升温速率为1℃/min,待加热完毕后,冷却至室温,得到最后的产物。First, fully mix nickel phthalocyanine, carbon nanotubes and anhydrous ethanol, the loading ratio of nickel phthalocyanine to precursor is 3%, and configure a mixed solution A of 2 mg/ml, and ultrasonicate the solution until no particles exist. After that, it was stirred for 12 hours, filtered with suction, and the reactant was obtained on qualitative filter paper. After the reactants are completely dried, the obtained reactants are calcined in a vacuum tube furnace. Generally, nitrogen or argon is used as a protective gas. The annealing temperature is 800°C, the holding time is 1h, and the heating rate is 1°C/min. After completion, cooling to room temperature yielded the final product.
实施例5Example 5
3%-800℃-Zn-NFC催化剂的制备Preparation of 3%-800℃-Zn-NFC catalyst
首先,把酞菁锌、氟化碳纳米管和无水乙醇充分混合,酞菁锌与前驱体的负载量比例为 3%,配置成2mg/ml的混合溶液A,将溶液超声至无颗粒存在后,搅拌12小时,抽滤,在定性滤纸上得到反应物。待反应物干燥完全,将得到的反应物放在真空管式炉中煅烧,一般使用氮气或氩气作为保护气体,退火温度为800℃,保温时间为1h,升温速率为1℃/min,待加热完毕后,冷却至室温,得到最后的产物。First, fully mix zinc phthalocyanine, carbon nanotubes and anhydrous ethanol, the loading ratio of zinc phthalocyanine to precursor is 3%, configure a mixed solution A of 2 mg/ml, and sonicate the solution until no particles exist. After that, it was stirred for 12 hours, filtered with suction, and the reactant was obtained on qualitative filter paper. After the reactants are completely dried, the obtained reactants are calcined in a vacuum tube furnace. Generally, nitrogen or argon is used as a protective gas. The annealing temperature is 800°C, the holding time is 1h, and the heating rate is 1°C/min. After completion, cooling to room temperature yielded the final product.
实施例6Example 6
3%-800℃-Mn-NFC催化剂的制备Preparation of 3%-800℃-Mn-NFC catalyst
首先,把酞菁锰、氟化碳纳米管和无水乙醇充分混合,酞菁锰与前驱体的负载量比例为 3%,配置成2mg/ml的混合溶液A,将溶液超声至无颗粒存在后,搅拌12小时,抽滤,在定性滤纸上得到反应物。待反应物干燥完全,将得到的反应物放在真空管式炉中煅烧,一般使用氮气或氩气作为保护气体,退火温度为800℃,保温时间为1h,升温速率为1℃/min,待加热完毕后,冷却至室温,得到最后的产物。First, fully mix manganese phthalocyanine, fluorinated carbon nanotubes and anhydrous ethanol, the loading ratio of manganese phthalocyanine to precursor is 3%, configure a mixed solution A of 2 mg/ml, and sonicate the solution until no particles exist. After that, it was stirred for 12 hours, filtered with suction, and the reactant was obtained on qualitative filter paper. After the reactants are completely dried, the obtained reactants are calcined in a vacuum tube furnace. Generally, nitrogen or argon is used as a protective gas. The annealing temperature is 800°C, the holding time is 1h, and the heating rate is 1°C/min. After completion, cooling to room temperature yielded the final product.
实施例7Example 7
5%-800℃-Co-NFC催化剂的制备Preparation of 5%-800℃-Co-NFC catalyst
首先,把酞菁钴、氟化碳纳米管和无水乙醇充分混合,酞菁钴与前驱体的负载量比例为 5%,配置成3mg/ml的混合溶液A,将溶液超声至无颗粒存在后,搅拌12小时,抽滤,在定性滤纸上得到反应物。待反应物干燥完全,将得到的反应物放在真空管式炉中煅烧,一般使用氮气或氩气作为保护气体,退火温度为800℃,保温时间为1h,升温速率为1℃/min,待加热完毕后,冷却至室温,得到最后的产物。First, mix cobalt phthalocyanine, fluorinated carbon nanotubes and anhydrous ethanol thoroughly. The loading ratio of cobalt phthalocyanine to the precursor is 5%, and configure a mixed solution A of 3 mg/ml. The solution is sonicated until no particles exist. After that, it was stirred for 12 hours, filtered with suction, and the reactant was obtained on qualitative filter paper. After the reactants are completely dried, the obtained reactants are calcined in a vacuum tube furnace. Generally, nitrogen or argon is used as a protective gas. The annealing temperature is 800°C, the holding time is 1h, and the heating rate is 1°C/min. After completion, cooling to room temperature yielded the final product.
实施例8Example 8
5%-800℃-Fe-NFC催化剂的制备Preparation of 5%-800℃-Fe-NFC catalyst
首先,把酞菁铁、氟化碳纳米管和无水乙醇充分混合,酞菁铁与前驱体的负载量比例为 5%,配置成3mg/ml的混合溶液A,将溶液超声至无颗粒存在后,搅拌12小时,抽滤,在定性滤纸上得到反应物。待反应物干燥完全,将得到的反应物放在真空管式炉中煅烧,一般使用氮气或氩气作为保护气体,退火温度为800℃,保温时间为1h,升温速率为1℃/min,待加热完毕后,冷却至室温,得到最后的产物。First, fully mix iron phthalocyanine, fluorinated carbon nanotubes and absolute ethanol, the loading ratio of iron phthalocyanine to the precursor is 5%, configure a mixed solution A of 3 mg/ml, and sonicate the solution until no particles exist. After that, it was stirred for 12 hours, filtered with suction, and the reactant was obtained on qualitative filter paper. After the reactants are completely dried, the obtained reactants are calcined in a vacuum tube furnace. Generally, nitrogen or argon is used as a protective gas. The annealing temperature is 800°C, the holding time is 1h, and the heating rate is 1°C/min. After completion, cooling to room temperature yielded the final product.
实施例9Example 9
5%-800℃-Cu-NFC催化剂的制备Preparation of 5%-800℃-Cu-NFC catalyst
首先,把酞菁铜、氟化碳纳米管和无水乙醇充分混合,酞菁铜与前驱体的负载量比例为 5%,配置成3mg/ml的混合溶液A,将溶液超声至无颗粒存在后,搅拌12小时,抽滤,在定性滤纸上得到反应物。待反应物干燥完全,将得到的反应物放在真空管式炉中煅烧,一般使用氮气或氩气作为保护气体,退火温度为800℃,保温时间为1h,升温速率为1℃/min,待加热完毕后,冷却至室温,得到最后的产物。First, fully mix copper phthalocyanine, carbon fluoride nanotubes and absolute ethanol, the loading ratio of copper phthalocyanine to precursor is 5%, prepare a mixed solution A of 3 mg/ml, and sonicate the solution until no particles exist. After that, it was stirred for 12 hours, filtered with suction, and the reactant was obtained on qualitative filter paper. After the reactants are completely dried, the obtained reactants are calcined in a vacuum tube furnace. Generally, nitrogen or argon is used as a protective gas. The annealing temperature is 800°C, the holding time is 1h, and the heating rate is 1°C/min. After completion, cooling to room temperature yielded the final product.
实施例10Example 10
5%-800℃-Zn-NFC催化剂的制备Preparation of 5%-800℃-Zn-NFC catalyst
首先,把酞菁锌、氟化碳纳米管和无水乙醇充分混合,酞菁锌与前驱体的负载量比例为 5%,配置成3mg/ml的混合溶液A,将溶液超声至无颗粒存在后,搅拌12小时,抽滤,在定性滤纸上得到反应物。待反应物干燥完全,将得到的反应物放在真空管式炉中煅烧,一般使用氮气或氩气作为保护气体,退火温度为800℃,保温时间为1h,升温速率为1℃/min,待加热完毕后,冷却至室温,得到最后的产物。First, fully mix zinc phthalocyanine, carbon nanotubes and anhydrous ethanol, the loading ratio of zinc phthalocyanine to precursor is 5%, configure a mixed solution A of 3 mg/ml, and sonicate the solution until no particles exist. After that, it was stirred for 12 hours, filtered with suction, and the reactant was obtained on qualitative filter paper. After the reactants are completely dried, the obtained reactants are calcined in a vacuum tube furnace. Generally, nitrogen or argon is used as a protective gas. The annealing temperature is 800°C, the holding time is 1h, and the heating rate is 1°C/min. After completion, cooling to room temperature yielded the final product.
实施例11Example 11
5%-800℃-Ni-NFC催化剂的制备Preparation of 5%-800℃-Ni-NFC catalyst
首先,把酞菁镍、氟化碳纳米管和无水乙醇充分混合,酞菁镍与前驱体的负载量比例为 5%,配置成3mg/ml的混合溶液A,将溶液超声至无颗粒存在后,搅拌12小时,抽滤,在定性滤纸上得到反应物。待反应物干燥完全,将得到的反应物放在真空管式炉中煅烧,一般使用氮气或氩气作为保护气体,退火温度为800℃,保温时间为1h,升温速率为1℃/min,待加热完毕后,冷却至室温,得到最后的产物。First, fully mix nickel phthalocyanine, carbon nanotubes and anhydrous ethanol, the loading ratio of nickel phthalocyanine to precursor is 5%, and configure a mixed solution A of 3 mg/ml, and sonicate the solution until no particles exist. After that, it was stirred for 12 hours, filtered with suction, and the reactant was obtained on qualitative filter paper. After the reactants are completely dried, the obtained reactants are calcined in a vacuum tube furnace. Generally, nitrogen or argon is used as a protective gas. The annealing temperature is 800°C, the holding time is 1h, and the heating rate is 1°C/min. After completion, cooling to room temperature yielded the final product.
实施例12Example 12
5%-800℃-Mn-NFC催化剂的制备Preparation of 5%-800℃-Mn-NFC catalyst
首先,把酞菁锰、氟化碳纳米管和无水乙醇充分混合,酞菁锰与载体的载量为5%,配置成3mg/ml的混合溶液A,将溶液超声至无颗粒存在后,搅拌12小时,抽滤,在定性滤纸上得到反应物。待反应物干燥完全,将得到的反应物放在真空管式炉中煅烧,一般使用氮气或氩气作为保护气体,退火温度为800℃,保温时间为1h,升温速率为1℃/min,待加热完毕后,冷却至室温,得到最后的产物。First, fully mix manganese phthalocyanine, fluorinated carbon nanotubes and absolute ethanol, the loading of manganese phthalocyanine and the carrier is 5%, and prepare a mixed solution A of 3 mg/ml. After the solution is sonicated until no particles exist, Stir for 12 hours, filter with suction, and obtain the reactant on qualitative filter paper. After the reactants are completely dried, the obtained reactants are calcined in a vacuum tube furnace. Generally, nitrogen or argon is used as a protective gas. The annealing temperature is 800°C, the holding time is 1h, and the heating rate is 1°C/min. After completion, cooling to room temperature yielded the final product.
实施例13Example 13
3%-500℃-Co-NFC催化剂的制备Preparation of 3%-500℃-Co-NFC catalyst
首先,把酞菁钴、氟化碳纳米管和无水乙醇充分混合,酞菁钴与前驱体的负载量比例为 3%,配置成2mg/ml的混合溶液A,将溶液超声至无颗粒存在后,搅拌12小时,抽滤,在定性滤纸上得到反应物。待反应物干燥完全,将得到的反应物放在真空管式炉中煅烧,一般使用氮气或氩气作为保护气体,退火温度为800℃,保温时间为1h,升温速率为1℃/min,待加热完毕后,冷却至室温,得到最后的产物。First, mix cobalt phthalocyanine, fluorinated carbon nanotubes and anhydrous ethanol thoroughly. The loading ratio of cobalt phthalocyanine to the precursor is 3%, and configure a mixed solution A of 2 mg/ml. The solution is sonicated until no particles exist. After that, it was stirred for 12 hours, filtered with suction, and the reactant was obtained on qualitative filter paper. After the reactants are completely dried, the obtained reactants are calcined in a vacuum tube furnace. Generally, nitrogen or argon is used as a protective gas. The annealing temperature is 800°C, the holding time is 1h, and the heating rate is 1°C/min. After completion, cooling to room temperature yielded the final product.
实施例14Example 14
3%-500℃-Fe-NFC催化剂的制备Preparation of 3%-500℃-Fe-NFC catalyst
首先,把酞菁铁、氟化碳纳米管和无水乙醇充分混合,酞菁铁与前驱体的负载量比例为 3%,配置成2mg/ml的混合溶液A,将溶液超声至无颗粒存在后,搅拌12小时,抽滤,在定性滤纸上得到反应物。待反应物干燥完全,将得到的反应物放在真空管式炉中煅烧,一般使用氮气或氩气作为保护气体,退火温度为800℃,保温时间为1h,升温速率为1℃/min,待加热完毕后,冷却至室温,得到最后的产物。First, fully mix iron phthalocyanine, fluorinated carbon nanotubes and anhydrous ethanol, the loading ratio of iron phthalocyanine to precursor is 3%, configure a mixed solution A of 2 mg/ml, and sonicate the solution until no particles exist. After that, it was stirred for 12 hours, filtered with suction, and the reactant was obtained on qualitative filter paper. After the reactants are completely dried, the obtained reactants are calcined in a vacuum tube furnace. Generally, nitrogen or argon is used as a protective gas. The annealing temperature is 800°C, the holding time is 1h, and the heating rate is 1°C/min. After completion, cooling to room temperature yielded the final product.
实施例15Example 15
3%-500℃-Cu-NFC催化剂的制备Preparation of 3%-500℃-Cu-NFC catalyst
首先,把酞菁铜、氟化碳纳米管和无水乙醇充分混合,酞菁铜与前驱体的负载量比例为 3%,配置成2mg/ml的混合溶液A,将溶液超声至无颗粒存在后,搅拌12小时,抽滤,在定性滤纸上得到反应物。待反应物干燥完全,将得到的反应物放在真空管式炉中煅烧,一般使用氮气或氩气作为保护气体,退火温度为800℃,保温时间为1h,升温速率为1℃/min,待加热完毕后,冷却至室温,得到最后的产物。First, fully mix copper phthalocyanine, carbon fluoride nanotubes and absolute ethanol, the loading ratio of copper phthalocyanine to precursor is 3%, configure a mixed solution A of 2 mg/ml, and sonicate the solution until no particles exist After that, it was stirred for 12 hours, filtered with suction, and the reactant was obtained on qualitative filter paper. After the reactants are completely dried, the obtained reactants are calcined in a vacuum tube furnace. Generally, nitrogen or argon is used as a protective gas. The annealing temperature is 800°C, the holding time is 1h, and the heating rate is 1°C/min. After completion, cooling to room temperature yielded the final product.
实施例16Example 16
3%-500℃-Zn-NFC催化剂的制备Preparation of 3%-500℃-Zn-NFC catalyst
首先,把酞菁锌、氟化碳纳米管和无水乙醇充分混合,酞菁锌与前驱体的负载量比例为 3%,配置成2mg/ml的混合溶液A,将溶液超声至无颗粒存在后,搅拌12小时,抽滤,在定性滤纸上得到反应物。待反应物干燥完全,将得到的反应物放在真空管式炉中煅烧,一般使用氮气或氩气作为保护气体,退火温度为800℃,保温时间为1h,升温速率为1℃/min,待加热完毕后,冷却至室温,得到最后的产物。First, fully mix zinc phthalocyanine, carbon nanotubes and anhydrous ethanol, the loading ratio of zinc phthalocyanine to precursor is 3%, configure a mixed solution A of 2 mg/ml, and sonicate the solution until no particles exist. After that, it was stirred for 12 hours, filtered with suction, and the reactant was obtained on qualitative filter paper. After the reactants are completely dried, the obtained reactants are calcined in a vacuum tube furnace. Generally, nitrogen or argon is used as a protective gas. The annealing temperature is 800°C, the holding time is 1h, and the heating rate is 1°C/min. After completion, cooling to room temperature yielded the final product.
实施例17Example 17
3%-500℃-Ni-NFC催化剂的制备Preparation of 3%-500℃-Ni-NFC catalyst
首先,把酞菁镍、氟化碳纳米管和无水乙醇充分混合,酞菁镍与前驱体的负载量比例为 3%,配置成2mg/ml的混合溶液A,将溶液超声至无颗粒存在后,搅拌12小时,抽滤,在定性滤纸上得到反应物。待反应物干燥完全,将得到的反应物放在真空管式炉中煅烧,一般使用氮气或氩气作为保护气体,退火温度为800℃,保温时间为1h,升温速率为1℃/min,待加热完毕后,冷却至室温,得到最后的产物。First, fully mix nickel phthalocyanine, carbon nanotubes and anhydrous ethanol, the loading ratio of nickel phthalocyanine to precursor is 3%, and configure a mixed solution A of 2 mg/ml, and ultrasonicate the solution until no particles exist. After that, it was stirred for 12 hours, filtered with suction, and the reactant was obtained on qualitative filter paper. After the reactants are completely dried, the obtained reactants are calcined in a vacuum tube furnace. Generally, nitrogen or argon is used as a protective gas. The annealing temperature is 800°C, the holding time is 1h, and the heating rate is 1°C/min. After completion, cooling to room temperature yielded the final product.
实施例18Example 18
3%-500℃-Mn-NFC催化剂的制备Preparation of 3%-500℃-Mn-NFC catalyst
首先,把酞菁锰、氟化碳纳米管和无水乙醇充分混合,酞菁锰与前驱体的负载量比例为 3%,配置成2mg/ml的混合溶液A,将溶液超声至无颗粒存在后,搅拌12小时,抽滤,在定性滤纸上得到反应物。待反应物干燥完全,将得到的反应物放在真空管式炉中煅烧,一般使用氮气或氩气作为保护气体,退火温度为800℃,保温时间为1h,升温速率为1℃/min,待加热完毕后,冷却至室温,得到最后的产物。First, fully mix manganese phthalocyanine, fluorinated carbon nanotubes and anhydrous ethanol, the loading ratio of manganese phthalocyanine to precursor is 3%, configure a mixed solution A of 2 mg/ml, and sonicate the solution until no particles exist. After that, it was stirred for 12 hours, filtered with suction, and the reactant was obtained on qualitative filter paper. After the reactants are completely dried, the obtained reactants are calcined in a vacuum tube furnace. Generally, nitrogen or argon is used as a protective gas. The annealing temperature is 800°C, the holding time is 1h, and the heating rate is 1°C/min. After completion, cooling to room temperature yielded the final product.
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112619683A (en) * | 2021-01-12 | 2021-04-09 | 南开大学 | g-C co-modified by iron phthalocyanine and tungsten oxide3N4Catalyst and preparation method thereof |
CN116024601A (en) * | 2022-12-28 | 2023-04-28 | 大连理工大学 | A carbon nanotube-based porous hollow fiber electrode for electrocatalytic reduction reaction and its application |
CN116237077A (en) * | 2023-03-20 | 2023-06-09 | 周口师范学院 | Method for synthesizing metal single-atom catalyst by using metal phthalocyanine compound |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AU753177B2 (en) * | 1999-05-28 | 2002-10-10 | University Of Dayton, The | Patterned carbon nanotube films |
CN102027621A (en) * | 2008-04-07 | 2011-04-20 | Acta股份公司 | High performance ORR (oxygen reduction reaction) PGM (pt group metal) free catalyst |
CN102569831A (en) * | 2012-03-07 | 2012-07-11 | 东华大学 | Carbon load copper phthalocyanine fuel cell catalyst CuPc/C and preparation method and application thereof |
KR20150067975A (en) * | 2013-12-11 | 2015-06-19 | 한국수자원공사 | Manufacturing method of cathode of microbial fuel cell and cathode of microbial fuel cell manufactured by the same |
CN109390596A (en) * | 2018-09-26 | 2019-02-26 | 北京化工大学 | A kind of iron-nitrogen-C catalyst preparation method and application |
CN110911694A (en) * | 2019-11-27 | 2020-03-24 | 南方科技大学 | Method for preparing heterogeneous single-molecule electrocatalyst using metal phthalocyanine molecule-nano-carbon and its application |
-
2020
- 2020-04-20 CN CN202010313678.0A patent/CN111644168A/en active Pending
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AU753177B2 (en) * | 1999-05-28 | 2002-10-10 | University Of Dayton, The | Patterned carbon nanotube films |
CN102027621A (en) * | 2008-04-07 | 2011-04-20 | Acta股份公司 | High performance ORR (oxygen reduction reaction) PGM (pt group metal) free catalyst |
CN102569831A (en) * | 2012-03-07 | 2012-07-11 | 东华大学 | Carbon load copper phthalocyanine fuel cell catalyst CuPc/C and preparation method and application thereof |
KR20150067975A (en) * | 2013-12-11 | 2015-06-19 | 한국수자원공사 | Manufacturing method of cathode of microbial fuel cell and cathode of microbial fuel cell manufactured by the same |
CN109390596A (en) * | 2018-09-26 | 2019-02-26 | 北京化工大学 | A kind of iron-nitrogen-C catalyst preparation method and application |
CN110911694A (en) * | 2019-11-27 | 2020-03-24 | 南方科技大学 | Method for preparing heterogeneous single-molecule electrocatalyst using metal phthalocyanine molecule-nano-carbon and its application |
Non-Patent Citations (2)
Title |
---|
KUN ZHAO: ""Enhanced H2O2production by selective electrochemical reduction of O2on fluorine-doped hierarchically porous carbon"", 《JOURNAL OF CATALYSIS》 * |
谢凯: "《新一代锂二次电池技术》", 31 August 2013, 国防工业出版社 * |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112619683A (en) * | 2021-01-12 | 2021-04-09 | 南开大学 | g-C co-modified by iron phthalocyanine and tungsten oxide3N4Catalyst and preparation method thereof |
CN116024601A (en) * | 2022-12-28 | 2023-04-28 | 大连理工大学 | A carbon nanotube-based porous hollow fiber electrode for electrocatalytic reduction reaction and its application |
CN116237077A (en) * | 2023-03-20 | 2023-06-09 | 周口师范学院 | Method for synthesizing metal single-atom catalyst by using metal phthalocyanine compound |
CN116237077B (en) * | 2023-03-20 | 2023-10-17 | 周口师范学院 | Method for synthesizing metal single-atom catalyst by using metal phthalocyanine compound |
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