WO2024000963A1 - Aluminum/carbon composite for hydrogen production by means of reaction with alkaline water, and preparation method therefor and use thereof - Google Patents

Aluminum/carbon composite for hydrogen production by means of reaction with alkaline water, and preparation method therefor and use thereof Download PDF

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WO2024000963A1
WO2024000963A1 PCT/CN2022/128472 CN2022128472W WO2024000963A1 WO 2024000963 A1 WO2024000963 A1 WO 2024000963A1 CN 2022128472 W CN2022128472 W CN 2022128472W WO 2024000963 A1 WO2024000963 A1 WO 2024000963A1
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aluminum
carbon
carbon composite
alkaline water
hydrogen production
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Chinese (zh)
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王平
玄登晖
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华南理工大学
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    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/06Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents
    • C01B3/08Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents with metals
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/06Combination of fuel cells with means for production of reactants or for treatment of residues
    • H01M8/0606Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants
    • H01M8/065Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants by dissolution of metals or alloys; by dehydriding metallic substances
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2002/00Crystal-structural characteristics
    • C01P2002/70Crystal-structural characteristics defined by measured X-ray, neutron or electron diffraction data
    • C01P2002/72Crystal-structural characteristics defined by measured X-ray, neutron or electron diffraction data by d-values or two theta-values, e.g. as X-ray diagram
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2002/00Crystal-structural characteristics
    • C01P2002/80Crystal-structural characteristics defined by measured data other than those specified in group C01P2002/70
    • C01P2002/82Crystal-structural characteristics defined by measured data other than those specified in group C01P2002/70 by IR- or Raman-data
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2004/00Particle morphology
    • C01P2004/01Particle morphology depicted by an image
    • C01P2004/03Particle morphology depicted by an image obtained by SEM
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2004/00Particle morphology
    • C01P2004/01Particle morphology depicted by an image
    • C01P2004/04Particle morphology depicted by an image obtained by TEM, STEM, STM or AFM
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/36Hydrogen production from non-carbon containing sources, e.g. by water electrolysis

Definitions

  • the invention belongs to the technical field of hydrogen production materials, and specifically relates to an aluminum/carbon composite that reacts with alkaline water to produce hydrogen and its preparation method and application.
  • Hydrogen is a clean and efficient energy carrier. Its large-scale industrial application is expected to fundamentally solve global problems such as energy shortage and environmental pollution. However, safe and efficient storage and transportation of hydrogen are still huge challenges facing the widespread application of hydrogen energy technology. challenge. Since around 2000, the use of hydrogen-rich materials/systems combined with spent fuel regeneration to produce hydrogen on demand has become a chemical hydrogen storage method for mobile or portable devices. Among the many candidate materials/systems, the aluminum-water system has attracted much attention due to its abundant resources, low reaction temperature, the generated hydrogen does not require purification, and the mature aluminum recycling technology.
  • the present invention proposes a method of using carbon materials as modifiers to compound with aluminum, thereby improving its hydrogen production performance in alkaline water.
  • the invention adopts a hydrogen production system and a hydrogen production method by reacting an aluminum/carbon composite with alkaline water.
  • the hydrogen production system consists of a solid composite and an alkaline liquid.
  • the weight ratio of the solid composite and the alkaline liquid is 1:5. ⁇ 1:1000; among them, the solid composite is an aluminum/carbon material composite.
  • the aluminum/carbon composite is prepared by mechanical ball milling.
  • the carbon is finely dispersed in the interior and surface of the aluminum matrix at micro-nano scale.
  • the composite has super affinity. Water-based, good antioxidant properties.
  • the aluminum/carbon composite that reacts with alkaline water to produce hydrogen.
  • the aluminum/carbon composite is composed of an aluminum matrix and a carbon material; the carbon material is dispersed and distributed on the surface of the aluminum matrix in the form of submicron or nanoscale particles. and internally, forming a continuous or quasi-continuous network.
  • the aluminum/carbon composite exhibits super hydrophilicity and good oxidation resistance.
  • the purity of the aluminum matrix is above 99%
  • the carbon material is one or a combination of one or more of carbon nanotubes, graphene, activated carbon, carbon fiber, graphite powder or conductive carbon black.
  • the above-mentioned preparation method of the aluminum/carbon composite for reacting with alkaline water to produce hydrogen includes the following steps:
  • step (1) Ball-mill the aluminum powder and the carbon material heat-treated in step (1) under a protective atmosphere to prepare an aluminum/carbon composite that reacts with alkaline water to produce hydrogen.
  • the protective atmosphere in step (1) is argon.
  • the heat treatment temperature in step (1) is 200-550°C
  • the time is 1-10 hours
  • the heating rate is 10°C/min.
  • the carbon material in step (1) is one or a combination of one or more of carbon nanotubes, graphene, activated carbon, carbon fiber, graphite powder or conductive carbon black.
  • the mass ratio of the aluminum powder and the heat-treated carbon material in step (2) is 1:1 ⁇ 100:1.
  • the mass ratio of the aluminum powder and the heat-treated carbon material in step (2) is 1:1 ⁇ 95:5.
  • the particle size of the aluminum powder in step (2) is 1 to 1000 ⁇ m.
  • the particle size of the aluminum powder in step (2) is 10 ⁇ 200 ⁇ m; the purity is 99.9%.
  • the diameter of the grinding ball used in the ball milling in step (2) is 5 mm-15 mm; the ball-to-material mass ratio of the grinding ball is 5:1 ⁇ 100:1.
  • the diameter of the grinding balls used in the ball milling in step (2) is 5, 10, or 15 mm;
  • the ball milling speed in step (2) is 100 to 2000 rpm, and the ball milling time is 1 minute to 50 hours.
  • the grinding jar and grinding balls of the ball mill in step (2) are agate, zirconia, cemented carbide, polyurethane or stainless steel; the protective atmosphere is argon.
  • the alkali in the alkaline water is one or a combination of sodium hydroxide (NaOH), potassium hydroxide (KOH), calcium hydroxide (Ca(OH) 2 ) or lithium hydroxide (LiOH).
  • the concentration of alkali is 0.1 ⁇ 10 M.
  • the concentration of the base is 0.5 ⁇ 5 M.
  • the weight ratio of the aluminum/carbon composite and alkaline water is 1:5 ⁇ 1:1000.
  • the hydrogen production reaction is carried out in a room temperature environment; the system temperature is not controlled during the hydrogen production reaction.
  • the design principle of the present invention is:
  • the key point is to have fast hydrogen production kinetics in a relatively mild solution without excessive modification costs. Previous studies often only considered the former and ignored the cost issue.
  • the aluminum/carbon composite provided by the present invention simultaneously solves these two problems to a certain extent.
  • the aluminum powder and carbon material are mechanically ball milled under the protection of an argon atmosphere.
  • the carbon material not only acts as a modifier, but also acts as a grinding aid to prevent the aluminum powder from adhering to each other due to cold welding during the ball milling process.
  • the carbon material is fully in contact with the aluminum matrix, which also creates a large number of interfaces, giving the aluminum/carbon composite a fluffy structure, providing a channel for moisture diffusion in the capillary effect, thereby increasing the contact area for the reaction.
  • the passivation film on the aluminum surface is destroyed and the following reaction occurs (1):
  • the present invention provides a modified new method suitable for hydrogen production from aluminum/water.
  • the key difference between this method and the traditional method is that the method is simple, easy to implement, fast and can be mass-produced. It significantly provides hydrogen production power. While learning, it also has low modification cost.
  • the physical mixing ability of the mechanical ball milling method is used to evenly distribute the carbon material on the surface and interior of the aluminum matrix, providing a large interface area and creating a channel for moisture diffusion, which is conducive to increasing the contact area of the reaction; in addition, by regulating the carbon material The proportion and ball milling time further strengthen the interaction between carbon and aluminum matrix, further improving the hydrogen production performance of the aluminum/carbon composite.
  • the aluminum/carbon composite material provided by the present invention and suitable for instant hydrogen production by mobile equipment uses cheap and easily available raw materials, has a simple preparation process, is pollution-free in the entire process, and is convenient for mass production.
  • the present invention provides an aluminum/carbon material-water composite system with high hydrogen production performance, which can achieve rapid hydrogen production kinetics at low alkali concentrations and has excellent oxidation resistance.
  • the comprehensive hydrogen production performance is currently at the top. level.
  • Figure 1b is a scanning electron microscope and the corresponding energy spectrum of the aluminum/carbon composite prepared in Example 1 after reacting in an alkali solution for 10 seconds.
  • Figure 5a is a hydrogen production kinetic curve of the aluminum/carbon composite prepared in Example 1 and pure aluminum powder in an alkaline solution.
  • Figure 5b is a hydrogen production rate curve over time of the aluminum/carbon composite prepared in Example 1 and pure aluminum powder in an alkaline solution.
  • Figure 8b is a hydrogen production rate curve as time changes in an alkali solution as the proportion of carbon material decreases in the aluminum/carbon composite prepared in Example 3 after ball milling for 15 minutes.
  • Figure 10a is a graph showing the change of the contact angle with time on the surface of the aluminum powder compact prepared in Example 5.
  • Figure 10b is a graph showing the change of contact angle with time on the surface of the Al/carbon composite tablet prepared in Example 5.
  • the generated hydrogen is cooled to room temperature through the condenser tube, and then collected in a gas collection bottle.
  • the amount of hydrogen produced is measured by the drainage method, and the hydrogen production volume-time curve is measured.
  • the measured hydrogen production volume is differentiated with time to obtain Hydrogen production rate-time curve.
  • Figure 5a and Figure 5b show the hydrogen production performance (including hydrogen production amount-time curve and hydrogen production rate-time curve) of aluminum/carbon composite and unmodified aluminum powder in alkaline solution.
  • the test results show that: It takes 8 minutes for the modified aluminum powder to achieve complete hydrogen production, and the maximum hydrogen production rate is only 251 mL min -1 g -1 ; while the modified aluminum/carbon composite can achieve complete hydrogen production within 1 minute. , the maximum hydrogen production rate reaches 4556 mL min -1 g -1 (based on the mass of aluminum/carbon composite), which is 18 times that of unmodified aluminum powder.
  • the hydrogen production method and hydrogen production performance test method are the same as in Example 1.
  • Figure 6a and Figure 6b show the comparison of hydrogen production performance of aluminum/carbon material composites in alkaline solution with different ball milling times. The results show that the hydrogen production kinetics of the aluminum/carbon material composite increases as the ball milling time increases, reaching a maximum at 15 minutes; when the ball milling time continues to be extended, the hydrogen production kinetics decrease.
  • the preparation of the Al/carbon composite is the same as in Example 1, except that the mass ratio of aluminum powder to carbon material is different.
  • the hydrogen production method and hydrogen production performance test method are the same as in Example 1.
  • Figure 8a and Figure 8b show the law of the hydrogen production performance curve (including hydrogen production amount-time curve and hydrogen production rate-time curve) when the proportion of carbon material in the aluminum/carbon composite in the alkaline solution continues to decrease: as the carbon material The proportion of carbon materials gradually decreases, and the hydrogen production kinetics gradually deteriorates, indicating that the higher the proportion of carbon materials, the better the modification effect on the aluminum matrix.
  • the Al/carbon composite preparation was the same as in Example 1.
  • the hydrogen production method and hydrogen production performance test method are the same as in Example 1.
  • the hydrogen production kinetics slowed down with the extension of storage time, and the maximum hydrogen production rate also decreased.
  • the hydrogen production kinetics and the maximum hydrogen production rate remained stable, and the sample still showed good performance.
  • the hydrogen production performance shows that the sample has certain antioxidant properties.
  • the Al/carbon composite preparation was the same as in Example 1.
  • Figure 10a and Figure 10b show the surface contact angle changes with time of aluminum powder tablets and Al/carbon composite tablets.
  • the surface contact angle of aluminum powder tablets is stable at 93°, showing hydrophobic characteristics; while water droplets After contacting the Al/carbon composite tablet, it is quickly absorbed and disappears within 0.05 seconds, showing super hydrophilicity.
  • the results of the examples show that the present invention adopts a modification method of mechanical ball milling of aluminum powder and carbon materials to promote hydrogen production from aluminum-water, which can solve the problems of low hydrogen production rate and high modification cost in the prior art.
  • the hydrogen system and hydrogen production method have the technical advantages of simple process, high efficiency, safety and low hydrogen production cost, and can provide a mobile hydrogen source for fuel cells of mobile or portable equipment.

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Abstract

Disclosed in the present invention are an aluminum/carbon composite for hydrogen production by means of reaction with alkaline water, and a preparation method therefor and the use thereof. The aluminum/carbon composite is composed of an aluminum matrix and a carbon material, wherein the carbon material is dispersively distributed on the surface and inside the aluminum matrix in the form of submicron or nanoscale particles, thereby forming a continuous or quasi-continuous network. In the present invention, by subjecting a carbon material to a heat treatment in a protective atmosphere and carrying out ball milling, in a protective atmosphere, on an aluminum powder and the carbon material, which has been subjected to the heat treatment, an aluminum/carbon composite for hydrogen production by means of reaction with alkaline water is prepared. In the preparation method provided in the present invention, the raw materials are easy to obtain, the operation is simple, and mass production is facilitated, such that the hydrogen production dynamics of an aluminum-water system can be significantly improved, a rapid reaction with alkaline water can be carried out in a room-temperature environment to produce hydrogen, and the highest hydrogen production rate thereof is located at the top level in the current reports.

Description

一种与碱性水反应制氢的铝/碳复合物及其制备方法与应用An aluminum/carbon composite that reacts with alkaline water to produce hydrogen and its preparation method and application 技术领域Technical field
本发明属于制氢材料技术领域,具体涉及一种与碱性水反应制氢的铝/碳复合物及其制备方法与应用。The invention belongs to the technical field of hydrogen production materials, and specifically relates to an aluminum/carbon composite that reacts with alkaline water to produce hydrogen and its preparation method and application.
背景技术Background technique
氢是一种清洁、高效的能源载体,其规模化产业应用有望根本性解决能源短缺、环境污染等全球性问题,但安全、高效地储存和运输氢仍是氢能技术广泛应用所面临的巨大挑战。自2000年前后,利用富氢材料/系统与乏燃料再生相结合,按需制氢,已经成为用于移动或便携设备的化学储氢方法。在众多的候选材料/体系中,铝-水体系因其资源丰富、反应温度低、生成的氢气无须纯化以及铝的循环利用技术成熟等特点而备受关注。Hydrogen is a clean and efficient energy carrier. Its large-scale industrial application is expected to fundamentally solve global problems such as energy shortage and environmental pollution. However, safe and efficient storage and transportation of hydrogen are still huge challenges facing the widespread application of hydrogen energy technology. challenge. Since around 2000, the use of hydrogen-rich materials/systems combined with spent fuel regeneration to produce hydrogen on demand has become a chemical hydrogen storage method for mobile or portable devices. Among the many candidate materials/systems, the aluminum-water system has attracted much attention due to its abundant resources, low reaction temperature, the generated hydrogen does not require purification, and the mature aluminum recycling technology.
然而铝表面连续致密钝化层的形成制约了铝-水体系作为氢源的应用潜力,针对这个问题,目前外国内外已经开发出多种改性手段,但都不能满足实际应用制氢的性能与成本需求。添加高浓度的碱性助剂,如氢氧化钠、氢氧化钾等,可以与氧化铝以及铝反应生成可溶性的偏铝酸盐化物,从而有效破坏钝化层的生成,但高的碱浓度又容易引发容器的应力腐蚀,对氢气发生器提出了苛刻的耐蚀性要求。采用镓、铟、锡、铋等低熔点金属与铝合金化可以通过削弱基体强度,改变钝化膜致密性等作用,从而实现在中性水中具备快速制氢性能(Studies on microstructure of activated aluminum and its hydrogen generation properties in aluminum/water reaction);但材料和改性成本的急剧升高,限制了这类铝基合金的实际应用。此外,铝与Al2O3,MgO等金属氧化物或NaCl,KCl等水溶性无机盐球磨也可以提升在其在中性水中的反应活性,但根据已发表的文献,在长时间的球磨过后,氧化物/盐对铝-水系统反应动力学的提升效果相当有限。因此,在不过度增加制备成本的前提下,探索先进的方法来解决铝-水系统的钝化问题仍然是当务之急。However, the formation of a continuous dense passivation layer on the aluminum surface restricts the application potential of the aluminum-water system as a hydrogen source. To address this problem, a variety of modification methods have been developed at home and abroad, but none of them can meet the performance and performance of hydrogen production in practical applications. cost requirements. Adding high-concentration alkaline additives, such as sodium hydroxide, potassium hydroxide, etc., can react with alumina and aluminum to form soluble metaaluminates, thereby effectively destroying the formation of the passivation layer, but high alkali concentrations It is easy to cause stress corrosion of the container, which imposes strict corrosion resistance requirements on the hydrogen generator. The use of low melting point metals such as gallium, indium, tin, and bismuth to alloy aluminum can achieve rapid hydrogen production performance in neutral water by weakening the strength of the matrix and changing the density of the passivation film (Studies on microstructure of activated aluminum and its hydrogen generation properties in aluminum/water reaction); however, the sharp increase in material and modification costs limits the practical application of this type of aluminum-based alloy. In addition, ball milling of aluminum with metal oxides such as Al2O3 and MgO or water-soluble inorganic salts such as NaCl and KCl can also improve its reactivity in neutral water. However, according to published literature, after long-term ball milling, the oxide /Salt has a rather limited effect on improving the reaction kinetics of the aluminum-water system. Therefore, it is still urgent to explore advanced methods to solve the passivation problem of aluminum-water systems without excessively increasing the preparation cost.
鉴于这种情况,本发明提出采用碳材料作为改性剂与铝复合的方法,从而提高其在碱性水中的制氢性能。In view of this situation, the present invention proposes a method of using carbon materials as modifiers to compound with aluminum, thereby improving its hydrogen production performance in alkaline water.
技术解决方案Technical solutions
针对现有技术存在的不足,本发明的目的在于提供一种适用于移动设备的与碱性水反应制氢的铝/碳复合物及其制备方法与应用(水反应制氢体系的制氢方法)。该制备方法原料易得、操作简便、便于量产、改性后的铝基复合物在低碱浓度下具备优异的制氢性能,可以解决现有技术中存在的制备成本过高、制氢速率低等问题。In view of the shortcomings of the existing technology, the purpose of the present invention is to provide an aluminum/carbon composite suitable for mobile equipment that reacts with alkaline water to produce hydrogen and its preparation method and application (hydrogen production method of water reaction hydrogen production system ). The preparation method has readily available raw materials, simple operation, and is convenient for mass production. The modified aluminum-based composite has excellent hydrogen production performance at low alkali concentration, and can solve the problems of high preparation cost and hydrogen production rate in the existing technology. Low question.
本发明采用铝/碳复合物与碱性水反应制氢体系和制氢方法,制氢体系由固体复合物和碱性液体两部分组成,固体复合物和碱性液体的重量比例在1:5~1:1000;其中,固体复合物为铝/碳材料复合物,铝/碳复合物采用机械球磨法制备,碳以微纳米尺度细小弥散的分散在铝基体内部和表面,复合物具有超亲水性,良好的抗氧化性。The invention adopts a hydrogen production system and a hydrogen production method by reacting an aluminum/carbon composite with alkaline water. The hydrogen production system consists of a solid composite and an alkaline liquid. The weight ratio of the solid composite and the alkaline liquid is 1:5. ~1:1000; among them, the solid composite is an aluminum/carbon material composite. The aluminum/carbon composite is prepared by mechanical ball milling. The carbon is finely dispersed in the interior and surface of the aluminum matrix at micro-nano scale. The composite has super affinity. Water-based, good antioxidant properties.
本发明的目的通过以下技术方案实现。The object of the present invention is achieved through the following technical solutions.
一种与碱性水反应制氢的铝/碳复合物,所述铝/碳复合物由铝基体和碳材料组成;所述碳材料以亚微米或纳米尺度的颗粒形式弥散分布于铝基体表面及内部,并形成了连续或准连续的网络。所述铝/碳复合物,表现出超亲水性及良好的抗氧化性。An aluminum/carbon composite that reacts with alkaline water to produce hydrogen. The aluminum/carbon composite is composed of an aluminum matrix and a carbon material; the carbon material is dispersed and distributed on the surface of the aluminum matrix in the form of submicron or nanoscale particles. and internally, forming a continuous or quasi-continuous network. The aluminum/carbon composite exhibits super hydrophilicity and good oxidation resistance.
优选的,所述铝基体的纯度为99%以上,碳材料为碳纳米管、石墨烯、活性炭、碳纤维、石墨粉或导电炭黑中一种或多种的组合。Preferably, the purity of the aluminum matrix is above 99%, and the carbon material is one or a combination of one or more of carbon nanotubes, graphene, activated carbon, carbon fiber, graphite powder or conductive carbon black.
优选的,所述铝/碳复合物具有多孔结构,孔尺寸为100 nm~10μm。Preferably, the aluminum/carbon composite has a porous structure with a pore size of 100 nm to 10 μm.
上述的与碱性水反应制氢的铝/碳复合物的制备方法,包含以下步骤:The above-mentioned preparation method of the aluminum/carbon composite for reacting with alkaline water to produce hydrogen includes the following steps:
(1)在保护气氛下将碳材料进行热处理;去除吸附的杂质气体与水分;所述碳材料热处理后,具有石墨碳和无定形碳两种相结构;(1) Heat-treat the carbon material under a protective atmosphere; remove adsorbed impurity gases and moisture; after heat treatment, the carbon material will have two phase structures: graphite carbon and amorphous carbon;
(2)将铝粉与步骤(1)热处理后的碳材料在保护气氛下进行球磨,制得与碱性水反应制氢的铝/碳复合物。(2) Ball-mill the aluminum powder and the carbon material heat-treated in step (1) under a protective atmosphere to prepare an aluminum/carbon composite that reacts with alkaline water to produce hydrogen.
优选的,步骤(1)所述的保护气氛为氩气。Preferably, the protective atmosphere in step (1) is argon.
优选的,步骤(1)所述热处理的温度为200~550℃,时间为1~10小时;升温速率为10℃/min。Preferably, the heat treatment temperature in step (1) is 200-550°C, the time is 1-10 hours, and the heating rate is 10°C/min.
优选的,步骤(1)所述碳材料为碳纳米管、石墨烯、活性炭、碳纤维、石墨粉或导电炭黑中一种或多种的组合。Preferably, the carbon material in step (1) is one or a combination of one or more of carbon nanotubes, graphene, activated carbon, carbon fiber, graphite powder or conductive carbon black.
优选的,步骤(2)所述铝粉与热处理后的碳材料的质量比为1:1~100:1。Preferably, the mass ratio of the aluminum powder and the heat-treated carbon material in step (2) is 1:1~100:1.
进一步优选的,步骤(2)所述铝粉与热处理后的碳材料的质量比为1:1~95:5。Further preferably, the mass ratio of the aluminum powder and the heat-treated carbon material in step (2) is 1:1~95:5.
优选的,步骤(2)所述铝粉的粒径1~1000μm。Preferably, the particle size of the aluminum powder in step (2) is 1 to 1000 μm.
进一步优选的,步骤(2)所述铝粉的粒径10~200μm;纯度为99.9%。Further preferably, the particle size of the aluminum powder in step (2) is 10~200 μm; the purity is 99.9%.
优选的,步骤(2)所述球磨所用的磨球的直径为5 mm-15 mm;所述磨球的球料质量比5:1~100:1。Preferably, the diameter of the grinding ball used in the ball milling in step (2) is 5 mm-15 mm; the ball-to-material mass ratio of the grinding ball is 5:1~100:1.
进一步优选的,步骤(2)所述球磨所用的磨球的直径为5 、10、15 mm;Further preferably, the diameter of the grinding balls used in the ball milling in step (2) is 5, 10, or 15 mm;
优选的,步骤(2)所述球磨的转速为100~2000转/分钟,球磨的时间为1分钟~50小时。Preferably, the ball milling speed in step (2) is 100 to 2000 rpm, and the ball milling time is 1 minute to 50 hours.
优选的,步骤(2)所述球磨的磨罐及磨球为玛瑙、氧化锆、硬质合金、聚氨酯或不锈钢;所述的保护气氛为氩气。Preferably, the grinding jar and grinding balls of the ball mill in step (2) are agate, zirconia, cemented carbide, polyurethane or stainless steel; the protective atmosphere is argon.
上述的与碱性水反应制氢的铝/碳复合物在与碱性水反应制氢中的应用。The application of the above-mentioned aluminum/carbon composite that reacts with alkaline water to produce hydrogen is used in reacting with alkaline water to produce hydrogen.
优选的,所述碱性水中的碱为氢氧化钠(NaOH)、氢氧化钾(KOH)、氢氧化钙(Ca(OH) 2)或氢氧化锂(LiOH)中一种或多种的组合,碱的浓度为0.1~10 M。 Preferably, the alkali in the alkaline water is one or a combination of sodium hydroxide (NaOH), potassium hydroxide (KOH), calcium hydroxide (Ca(OH) 2 ) or lithium hydroxide (LiOH). , the concentration of alkali is 0.1~10 M.
进一步优选的,碱的浓度为0.5~5 M。Further preferably, the concentration of the base is 0.5~5 M.
优选的,所述铝/碳复合物和碱性水的重量比为1:5~1:1000。Preferably, the weight ratio of the aluminum/carbon composite and alkaline water is 1:5~1:1000.
优选的,制氢反应在室温环境中进行;制氢反应过程中不对体系温度进行控制。Preferably, the hydrogen production reaction is carried out in a room temperature environment; the system temperature is not controlled during the hydrogen production reaction.
本发明的设计原理是:The design principle of the present invention is:
对于铝水反应制氢改性方法,关键点是在相对温和的溶液中具备快速制氢动力学,并且无需过高的改性成本。以往的研究往往只考虑前者而忽略了成本问题,而本发明所提供的铝/碳复合物同时对这两个问题进行了一定程度上的解决。首先,将铝粉和碳材料在氩气氛保护下机械球磨,在这个过程,碳材料不仅充当改性剂,而且还可以充当助磨剂防止铝粉在球磨过程中由冷焊现象导致的相互粘连;此外,碳材料与铝基体充分地接触,也创造了大量的界面,使铝/碳复合物具备蓬松的结构,提供了毛细效应中水分扩散的通道,进而增大了反应的接触面积,当接触到碱溶液时,铝表面的钝化膜被破坏,发生如下反应 (1):For the aluminum-water reaction hydrogen production modification method, the key point is to have fast hydrogen production kinetics in a relatively mild solution without excessive modification costs. Previous studies often only considered the former and ignored the cost issue. However, the aluminum/carbon composite provided by the present invention simultaneously solves these two problems to a certain extent. First, the aluminum powder and carbon material are mechanically ball milled under the protection of an argon atmosphere. In this process, the carbon material not only acts as a modifier, but also acts as a grinding aid to prevent the aluminum powder from adhering to each other due to cold welding during the ball milling process. ; In addition, the carbon material is fully in contact with the aluminum matrix, which also creates a large number of interfaces, giving the aluminum/carbon composite a fluffy structure, providing a channel for moisture diffusion in the capillary effect, thereby increasing the contact area for the reaction. When exposed to an alkali solution, the passivation film on the aluminum surface is destroyed and the following reaction occurs (1):
Al 2O 3 + 3H 2O + 2OH - → 2[Al(OH) 4] -                          (1) Al 2 O 3 + 3H 2 O + 2OH - → 2[Al(OH) 4 ] - (1)
随后渗透进铝/碳复合物的碱性水溶液接触到铝基体,发生反应 (2)The alkaline aqueous solution that then penetrates into the aluminum/carbon composite contacts the aluminum matrix and reacts (2)
2Al + 6H 2O + 2OH - → 2[Al(OH) 4] -  + 3H 2↑                        (2) 2Al + 6H 2 O + 2OH - → 2[Al(OH) 4 ] - + 3H 2 ↑ (2)
有益效果beneficial effects
本发明的优点及有益效果在于:The advantages and beneficial effects of the present invention are:
(1) 本发明提供了适用于铝/水制氢的改性新方法,该刚发区别于传统方法的关键之处在于方法简单易行,快速且可大量生产,在显著提供了制氢动力学的同时兼具低改性成本。利用机械球磨法的物理混合能力,使碳材料均匀地分布于铝基体的表面及内部,提供大量的界面面积,创造了水分扩散的通道,有利于提高反应的接触面积;此外通过调控碳材料所占的比例与球磨时间进一步强化碳与铝基体的相互作用,进一步改善铝/碳复合物的制氢性能。(1) The present invention provides a modified new method suitable for hydrogen production from aluminum/water. The key difference between this method and the traditional method is that the method is simple, easy to implement, fast and can be mass-produced. It significantly provides hydrogen production power. While learning, it also has low modification cost. The physical mixing ability of the mechanical ball milling method is used to evenly distribute the carbon material on the surface and interior of the aluminum matrix, providing a large interface area and creating a channel for moisture diffusion, which is conducive to increasing the contact area of the reaction; in addition, by regulating the carbon material The proportion and ball milling time further strengthen the interaction between carbon and aluminum matrix, further improving the hydrogen production performance of the aluminum/carbon composite.
(2) 本发明提供的适用于移动设备即时制氢的铝/碳复合材料采用的原材料廉价易得,制备工艺简单、全程无污染、便于量产。(2) The aluminum/carbon composite material provided by the present invention and suitable for instant hydrogen production by mobile equipment uses cheap and easily available raw materials, has a simple preparation process, is pollution-free in the entire process, and is convenient for mass production.
(3) 本发明提供了高制氢性能铝/碳材料-水复合体系,可在低碱浓度下实现快速的制氢动力学,且具有优异的抗氧化性,综合制氢性能位于目前的顶尖水平。(3) The present invention provides an aluminum/carbon material-water composite system with high hydrogen production performance, which can achieve rapid hydrogen production kinetics at low alkali concentrations and has excellent oxidation resistance. The comprehensive hydrogen production performance is currently at the top. level.
附图说明Description of the drawings
图1a为实施例1制备的球磨15分钟Al:碳材料=5的铝/碳复合物制备态的扫描电镜及对应的能谱图。Figure 1a is a scanning electron microscope and the corresponding energy spectrum of the aluminum/carbon composite prepared in Example 1 after ball milling for 15 minutes: Al: carbon material = 5.
图1b为实施例1制备的铝/碳复合物在碱溶液中反应10秒后的扫描电镜及对应的能谱图。Figure 1b is a scanning electron microscope and the corresponding energy spectrum of the aluminum/carbon composite prepared in Example 1 after reacting in an alkali solution for 10 seconds.
图2a为实施例1制备的球磨15分钟Al:碳材料=5的铝/碳复合物高脚环形暗场透射电镜及对应的能谱分析图。Figure 2a is a high-leg annular dark field transmission electron microscope and the corresponding energy spectrum analysis chart of the aluminum/carbon composite prepared in Example 1 after ball milling for 15 minutes with Al:carbon material = 5.
图2b为实施例1制备的球磨15分钟Al:碳材料=5的铝/碳复合物透射电镜及对应区域的电子衍射图片。Figure 2b is a transmission electron microscope and electron diffraction picture of the corresponding area of the aluminum/carbon composite prepared in Example 1 after ball milling for 15 minutes with Al:carbon material = 5.
图2c为实施例1制备的球磨15分钟Al:碳材料=5的铝/碳复合物高分辨透射电镜结果图。Figure 2c is a high-resolution transmission electron microscope result of the aluminum/carbon composite prepared in Example 1 after ball milling for 15 minutes with Al:carbon material = 5.
图3为实施例1制备的球磨15分钟Al:碳材料=5的铝/碳复合物的XRD图。Figure 3 is the XRD pattern of the aluminum/carbon composite prepared in Example 1 after ball milling for 15 minutes with Al:carbon material = 5.
图4为实施例1制备的球磨15分钟Al:碳材料=5的铝/碳复合物的拉曼光谱。Figure 4 is the Raman spectrum of the aluminum/carbon composite prepared in Example 1 after ball milling for 15 minutes with Al:carbon material = 5.
图5a为实施例1制备的铝/碳复合物与纯铝粉在碱溶液中的制氢动力学曲线。Figure 5a is a hydrogen production kinetic curve of the aluminum/carbon composite prepared in Example 1 and pure aluminum powder in an alkaline solution.
图5b为实施例1制备的铝/碳复合物与纯铝粉在碱溶液中的随时间变化的的制氢速率曲线。Figure 5b is a hydrogen production rate curve over time of the aluminum/carbon composite prepared in Example 1 and pure aluminum powder in an alkaline solution.
图6a为实施例2制备的不同球磨时间的Al:碳材料=5的铝/碳复合物在碱溶液中的制氢动力学曲线。Figure 6a is the hydrogen production kinetic curve of the aluminum/carbon composite prepared in Example 2 with different ball milling times of Al: carbon material = 5 in an alkaline solution.
图6b为实施例2制备的不同球磨时间的Al:碳材料=5的铝/碳复合物在碱溶液中的随时间变化的的制氢速率曲线。Figure 6b shows the hydrogen production rate curve of the aluminum/carbon composite prepared in Example 2 with different ball milling times of Al: carbon material = 5 in an alkaline solution as a function of time.
图7a为实施例2制备的球磨10分钟的Al:碳材料=5的铝/碳复合物扫描电镜及对应能的谱分析图。Figure 7a is a scanning electron microscope and corresponding energy spectrum analysis chart of the aluminum/carbon composite of Al: carbon material = 5 that was ball-milled for 10 minutes prepared in Example 2.
图7b为实施例2制备的球磨20分钟的Al:碳材料=5的铝/碳复合物扫描电镜及对应能的谱分析图。Figure 7b is a scanning electron microscope and corresponding energy spectrum analysis chart of the aluminum/carbon composite of Al: carbon material = 5 that was ball-milled for 20 minutes prepared in Example 2.
图7c为实施例2制备的球磨1小时的Al:碳材料=5的铝/碳复合物扫描电镜及对应能的谱分析图。Figure 7c is a scanning electron microscope and corresponding energy spectrum analysis chart of the aluminum/carbon composite of Al: carbon material = 5 that was ball-milled for 1 hour prepared in Example 2.
图8a为实施例3制备的球磨15分钟铝/碳复合物中随碳材料比例降低在碱溶液中的制氢动力学曲线。Figure 8a is a kinetic curve of hydrogen production in an alkaline solution as the proportion of carbon material decreases in the ball-milled aluminum/carbon composite prepared in Example 3 for 15 minutes.
图8b为实施例3制备的球磨15分钟铝/碳复合物中随碳材料比例降低在碱溶液中的随时间变化的的制氢速率曲线。Figure 8b is a hydrogen production rate curve as time changes in an alkali solution as the proportion of carbon material decreases in the aluminum/carbon composite prepared in Example 3 after ball milling for 15 minutes.
图9a为实施例4制备的球磨15分钟Al:碳材料=5的铝/碳复合物随着在空气中放置时间延长在碱溶液中的制氢动力学曲线。Figure 9a shows the hydrogen production kinetic curve of the aluminum/carbon composite prepared in Example 4 after ball milling for 15 minutes with Al:carbon material = 5 as the time left in the air increases in an alkali solution.
图9b为实施例4制备的球磨15分钟Al:碳材料=5的铝/碳复合物随着在空气中放置时间延长在碱溶液中的随时间变化的的制氢速率曲线。Figure 9b shows the hydrogen production rate curve of the aluminum/carbon composite prepared in Example 4 that was ball-milled for 15 minutes with Al:carbon material = 5 and placed in the air for longer in an alkaline solution.
图10a为实施例5制备的铝粉压片表面接触角随时间的变化图。Figure 10a is a graph showing the change of the contact angle with time on the surface of the aluminum powder compact prepared in Example 5.
图10b为实施例5制备的Al/碳复合物压片表面接触角随时间的变化图。Figure 10b is a graph showing the change of contact angle with time on the surface of the Al/carbon composite tablet prepared in Example 5.
本发明的实施方式Embodiments of the invention
以下结合附图和实施例对本发明的具体实施作进一步说明,但本发明的实施和保护不限于此。需指出的是,以下若有未特别详细说明之过程,均是本领域技术人员可参照现有技术实现或理解的。所用试剂或仪器未注明生产厂商者,视为可以通过市售购买得到的常规产品。The specific implementation of the present invention will be further described below in conjunction with the accompanying drawings and examples, but the implementation and protection of the present invention are not limited thereto. It should be pointed out that any process that is not specifically described in detail below can be implemented or understood by those skilled in the art with reference to the existing technology. If the manufacturer of the reagents or instruments used is not indicated, they are regarded as conventional products that can be purchased commercially.
实施例Example 11
Al/碳复合物的合成、结构与制氢性能Synthesis, structure and hydrogen production performance of Al/carbon composites
Al/碳复合物制备Al/carbon composite preparation
选取所应用的碳材料(活性碳)将其在氩气氛下加热至400 ℃,升温速率10 ℃/分钟,经3小时恒温处理后随炉冷却至室温。随后在手套箱中将粒径25μm的铝粉、热处理后的碳材料与磨球(5mm,10mm,15mm的磨球按照质量比为5:2:1混合)按照1:30的质量比装入球磨罐,铝粉与碳材料质量比为5:1,在1000转每分钟的转速下球磨15分钟,制得目标铝/碳复合物。Select the carbon material (activated carbon) to be used and heat it to 400°C under an argon atmosphere. ℃, the heating rate is 10 ℃/min, and after 3 hours of constant temperature treatment, it is cooled to room temperature in the furnace. Then, put aluminum powder with a particle size of 25 μm, heat-treated carbon materials and grinding balls (5mm, 10mm, and 15mm grinding balls are mixed at a mass ratio of 5:2:1) into the glove box at a mass ratio of 1:30. In the ball milling tank, the mass ratio of aluminum powder to carbon material is 5:1, and the ball is milled at 1000 rpm for 15 minutes to obtain the target aluminum/carbon composite.
铝/碳复合物的物相/结构表征:Phase/structural characterization of aluminum/carbon composites:
扫描电镜观察以及对应的能谱分析(图1a和图1b)发现:机械球磨后,大量不同尺寸的碳颗粒镶嵌在铝基体上,但在反应进行10秒后再次对样品进行观察,发现碳颗粒大量从铝基体上脱落,铝基体上出现了脱嵌形成的凹坑。Scanning electron microscopy observation and corresponding energy spectrum analysis (Figure 1a and Figure 1b) found that after mechanical ball milling, a large number of carbon particles of different sizes were embedded in the aluminum matrix. However, the sample was observed again after 10 seconds of reaction and carbon particles were found. A large amount of chips fell off the aluminum base, and pits formed by de-embedding appeared on the aluminum base.
高脚环形暗场透射电镜观察及对应的能谱分析(图2a)进一步确认了铝碳在亚微米到纳米尺度的均匀复合,碳材料在铝基体中形成了连续或准连续的网络。选取电子衍射(图2b)确认了铝的衍射环,高分辨透射电子显微镜观察(图2c)到了碳材料中的特征非晶碳形貌。High-leg annular dark field transmission electron microscopy observation and corresponding energy spectrum analysis (Figure 2a) further confirmed the uniform composite of aluminum and carbon at the submicron to nanometer scale, and the carbon material formed a continuous or quasi-continuous network in the aluminum matrix. Electron diffraction (Figure 2b) was selected to confirm the diffraction ring of aluminum, and high-resolution transmission electron microscopy (Figure 2c) observed the characteristic amorphous carbon morphology in carbon materials.
XRD分析(图3)显示了清晰指认的铝的尖锐衍射峰,以及碳材料对应的非晶峰。XRD analysis (Figure 3) shows clearly identified sharp diffraction peaks of aluminum and corresponding amorphous peaks of carbon materials.
拉曼光谱(图4)出现的D峰和G峰以及I D/I G=1.06同样证明了以非晶碳为主要组成相的碳材料的存在。 The D and G peaks and I D /I G =1.06 appearing in the Raman spectrum (Figure 4) also prove the existence of carbon materials with amorphous carbon as the main component phase.
制氢方法:Hydrogen production method:
在室温环境下(25 ℃)将1 g铝/碳复合物置于两颈烧瓶中,通过恒压漏斗将1 M NaOH 溶液100 mL注入两颈烧瓶,反应过程中不对体系温度进行控制。(以铝粉作为对比实验)Place 1 g of aluminum/carbon composite into a two-necked flask at room temperature (25°C), and inject 100 mL of 1 M NaOH solution into the two-necked flask through a constant pressure funnel. The system temperature is not controlled during the reaction. (Using aluminum powder as a comparative experiment)
制氢性能测试:Hydrogen production performance test:
产生的氢气通过冷凝管冷却至室温,后经过集气瓶收集,并通过排水法测量产生氢气的量,测得制氢量-时间曲线;将测得的制氢量对时间进行微分,测得制氢速率-时间曲线。The generated hydrogen is cooled to room temperature through the condenser tube, and then collected in a gas collection bottle. The amount of hydrogen produced is measured by the drainage method, and the hydrogen production volume-time curve is measured. The measured hydrogen production volume is differentiated with time to obtain Hydrogen production rate-time curve.
图5a和图5b给出了铝/碳复合物与未经改性铝粉在碱溶液中的制氢性能(包括制氢量-时间曲线及制氢速率-时间曲线),测试结果表明:未经改性的铝粉要经过8分钟才能实现完全制氢,最高制氢速率仅为251 mL min -1g -1 ;而改性后的铝/碳复合物可以实现1分钟之内完全制氢,最高制氢速率达到4556 mL min -1g -1(以铝/碳复合物的质量计),是未改性铝粉的18倍。 Figure 5a and Figure 5b show the hydrogen production performance (including hydrogen production amount-time curve and hydrogen production rate-time curve) of aluminum/carbon composite and unmodified aluminum powder in alkaline solution. The test results show that: It takes 8 minutes for the modified aluminum powder to achieve complete hydrogen production, and the maximum hydrogen production rate is only 251 mL min -1 g -1 ; while the modified aluminum/carbon composite can achieve complete hydrogen production within 1 minute. , the maximum hydrogen production rate reaches 4556 mL min -1 g -1 (based on the mass of aluminum/carbon composite), which is 18 times that of unmodified aluminum powder.
性能测试结果表明:铝粉与碳材料经过机械球磨改性后,在低碱浓度环境中的制氢动力学得到了显著的提升。Performance test results show that after the aluminum powder and carbon materials are modified by mechanical ball milling, the hydrogen production kinetics in a low alkali concentration environment has been significantly improved.
实施例Example 22
球磨时间对铝/碳材料复合物制氢性能的影响、铝/碳材料复合物的微观结构随球磨时间的变化。The effect of ball milling time on the hydrogen production performance of aluminum/carbon material composites, and the changes in the microstructure of aluminum/carbon material composites with ball milling time.
Al/碳复合物制备与实施例1相同,区别仅在于球磨时间不同。The preparation of the Al/carbon composite was the same as in Example 1, the only difference being that the ball milling time was different.
制氢方法及制氢性能测试方法同实施例1。The hydrogen production method and hydrogen production performance test method are the same as in Example 1.
图6a和图6b给出了不同球磨时间铝/碳材料复合物在碱溶液中的制氢性能对比情况。结果显示,铝/碳材料复合物的制氢动力学随着球磨时间的增长而升高,在到达15分钟时达到最高;当继续延长球磨时间时,却导致了制氢动力学的下降。Figure 6a and Figure 6b show the comparison of hydrogen production performance of aluminum/carbon material composites in alkaline solution with different ball milling times. The results show that the hydrogen production kinetics of the aluminum/carbon material composite increases as the ball milling time increases, reaching a maximum at 15 minutes; when the ball milling time continues to be extended, the hydrogen production kinetics decrease.
不同球磨时间铝/碳复合物的形貌表征Morphological characterization of aluminum/carbon composites at different ball milling times
根据扫描电镜结合能谱分析(图7a、图7b和图7c)发现,碳颗粒随着球磨时间的延长逐渐破碎,并镶嵌在铝基体上,阻止了铝表面钝化膜的生成,同时为水分子进入铝基体内部提供了窗口和扩散通道;但由于纯铝具有良好的塑性和形变能力,碳颗粒很快在铝相互焊合粘连的的过程中被包覆在基体内部。(能谱中碳信号逐渐减弱乃至消失)According to scanning electron microscopy combined with energy spectroscopy analysis (Figure 7a, Figure 7b and Figure 7c), it was found that the carbon particles gradually fragmented as the ball milling time increased and were embedded in the aluminum matrix, preventing the formation of a passivation film on the aluminum surface and at the same time providing water Windows and diffusion channels are provided for molecules to enter the interior of the aluminum matrix; however, due to the good plasticity and deformation ability of pure aluminum, the carbon particles are quickly coated inside the matrix during the process of welding and adhering the aluminum to each other. (The carbon signal in the energy spectrum gradually weakens or even disappears)
实施例Example 33
碳材料比例对铝/碳复合物制氢性能的影响。Effect of carbon material ratio on hydrogen production performance of aluminum/carbon composites.
Al/碳复合物制备与实施例1相同,区别仅在于铝粉与碳材料质量比不同。The preparation of the Al/carbon composite is the same as in Example 1, except that the mass ratio of aluminum powder to carbon material is different.
制氢方法及制氢性能测试方法同实施例1。The hydrogen production method and hydrogen production performance test method are the same as in Example 1.
图8a和图8b给出了在碱溶液中铝/碳复合物中碳材料比例不断降低制氢性能曲线的规律(包括制氢量-时间曲线及制氢速率-时间曲线):随着碳材料的比例逐渐降低,制氢动力学逐渐变差,说明碳材料的比例越高,对铝基体的改性效果越好。Figure 8a and Figure 8b show the law of the hydrogen production performance curve (including hydrogen production amount-time curve and hydrogen production rate-time curve) when the proportion of carbon material in the aluminum/carbon composite in the alkaline solution continues to decrease: as the carbon material The proportion of carbon materials gradually decreases, and the hydrogen production kinetics gradually deteriorates, indicating that the higher the proportion of carbon materials, the better the modification effect on the aluminum matrix.
实施例Example 44
在空气中放置对铝/碳复合物制氢性能的影响。Effect of exposure to air on hydrogen production performance of aluminum/carbon composites.
Al/碳复合物制备与实施例1相同。The Al/carbon composite preparation was the same as in Example 1.
制氢方法及制氢性能测试方法同实施例1。The hydrogen production method and hydrogen production performance test method are the same as in Example 1.
图9a和图9b给出了在碱溶液中Al:碳材料=5的铝/碳复合物随着在空气中放置时间的延长制氢性能的变化(包括制氢量-时间曲线及制氢速率-时间曲线)。制氢动力学随着放置时间的延长而有减慢,最高制氢速率也随之下降,但放置时间到达12小时后,制氢动力学与最高制氢速率保持稳定,样品依旧表现出了良好的制氢性能,这表明样品有一定的抗氧化性能。Figure 9a and Figure 9b show the changes in hydrogen production performance of the aluminum/carbon composite with Al:carbon material = 5 in alkaline solution as the time left in the air increases (including hydrogen production amount-time curve and hydrogen production rate -time curve). The hydrogen production kinetics slowed down with the extension of storage time, and the maximum hydrogen production rate also decreased. However, after the storage time reached 12 hours, the hydrogen production kinetics and the maximum hydrogen production rate remained stable, and the sample still showed good performance. The hydrogen production performance shows that the sample has certain antioxidant properties.
实施例Example 55
Al/碳复合物的亲水性测试Hydrophilicity test of Al/carbon composites
Al/碳复合物制备与实施例1相同。The Al/carbon composite preparation was the same as in Example 1.
使用压片机将相同质量未经处理的铝粉与Al/碳复合物分别压制为直径为10 mm,厚度1 mm的圆形压片,进行表面接触角测试。Use a tablet press to press the same quality of untreated aluminum powder and Al/carbon composite into circular tablets with a diameter of 10 mm and a thickness of 1 mm, and conduct surface contact angle tests.
图10a和图10b给出了铝粉压片及Al/碳复合物压片的表面接触角随时间的变化,铝粉压片的表面接触角稳定在93°,表现出疏水的特性;而水滴在接触到Al/碳复合物压片0.05秒以内就迅速被压片所吸收而消失,表现出超亲水性。Figure 10a and Figure 10b show the surface contact angle changes with time of aluminum powder tablets and Al/carbon composite tablets. The surface contact angle of aluminum powder tablets is stable at 93°, showing hydrophobic characteristics; while water droplets After contacting the Al/carbon composite tablet, it is quickly absorbed and disappears within 0.05 seconds, showing super hydrophilicity.
实施例的结果表明:本发明采用将铝粉与碳材料机械球磨促进铝-水制氢的改性方法,可以解决现有技术中存在的制氢速率低、改性成本过高等问题,该制氢体系及制氢方法具有工艺简单、高效、安全且制氢成本较低等技术优点,可为移动或便携设备的燃料电池提供移动氢源。The results of the examples show that the present invention adopts a modification method of mechanical ball milling of aluminum powder and carbon materials to promote hydrogen production from aluminum-water, which can solve the problems of low hydrogen production rate and high modification cost in the prior art. The hydrogen system and hydrogen production method have the technical advantages of simple process, high efficiency, safety and low hydrogen production cost, and can provide a mobile hydrogen source for fuel cells of mobile or portable equipment.
以上实施例为本发明较佳的实施方式,但本发明的实施方式并不受上述实施例的限制,其他的任何未背离本发明的精神实质与原理下所作的改变、修饰、替代、组合、简化,均应为等效的置换方式,都包含在本发明的保护范围之内。The above embodiments are preferred embodiments of the present invention, but the embodiments of the present invention are not limited by the above embodiments. Any other changes, modifications, substitutions, combinations, etc. may be made without departing from the spirit and principles of the present invention. All simplifications should be equivalent substitutions, and are all included in the protection scope of the present invention.

Claims (10)

  1. 一种与碱性水反应制氢的铝/碳复合物,其特征在于,所述铝/碳复合物由铝基体和碳材料组成;所述碳材料以亚微米或纳米尺度的颗粒形式弥散分布于铝基体表面及内部,并形成了连续或准连续的网络。 An aluminum/carbon composite that reacts with alkaline water to produce hydrogen, characterized in that the aluminum/carbon composite is composed of an aluminum matrix and a carbon material; the carbon material is dispersed in the form of submicron or nanoscale particles. On the surface and inside of the aluminum matrix, a continuous or quasi-continuous network is formed.
  2. 根据权利要求1所述的与碱性水反应制氢的铝/碳复合物,其特征在于,所述铝基体的纯度为99%以上,碳材料为碳纳米管、石墨烯、活性炭、碳纤维、石墨粉或导电炭黑中一种或多种的组合。 The aluminum/carbon composite that reacts with alkaline water to produce hydrogen according to claim 1, wherein the purity of the aluminum matrix is more than 99%, and the carbon material is carbon nanotubes, graphene, activated carbon, carbon fiber, One or a combination of graphite powder or conductive carbon black.
  3. 权利要求1或2所述的与碱性水反应制氢的铝/碳复合物的制备方法,其特征在于,包含以下步骤: The preparation method of an aluminum/carbon composite for reacting with alkaline water to produce hydrogen according to claim 1 or 2, characterized in that it includes the following steps:
    (1)在保护气氛下将碳材料进行热处理;(1) Heat treatment of carbon materials in a protective atmosphere;
    (2)将铝粉与步骤(1)热处理后的碳材料在保护气氛下进行球磨,制得与碱性水反应制氢的铝/碳复合物。(2) Ball-mill the aluminum powder and the carbon material heat-treated in step (1) under a protective atmosphere to prepare an aluminum/carbon composite that reacts with alkaline water to produce hydrogen.
  4. 根据权利要求3所述的与碱性水反应制氢的铝/碳复合物的制备方法,其特征在于:步骤(1)所述的保护气氛为氩气;所述热处理的温度为200~550 ℃,时间为1~10小时。 The method for preparing an aluminum/carbon composite that reacts with alkaline water to produce hydrogen according to claim 3, characterized in that: the protective atmosphere in step (1) is argon; the temperature of the heat treatment is 200~550 ℃, time is 1~10 hours.
  5. 根据权利要求3所述的与碱性水反应制氢的铝/碳复合物的制备方法,其特征在于:步骤(2)所述铝粉与热处理后的碳材料的质量比为1:1~100:1;所述铝粉的粒径1~1000 μm。 The method for preparing an aluminum/carbon composite that reacts with alkaline water to produce hydrogen according to claim 3, characterized in that: the mass ratio of the aluminum powder in step (2) to the heat-treated carbon material is 1:1~ 100:1; the particle size of the aluminum powder is 1~1000 μm.
  6. 根据权利要求3所述的与碱性水反应制氢的铝/碳复合物的制备方法,其特征在于:步骤(2)所述球磨所用的磨球的直径为5 mm-15 mm;所述磨球的球料质量比5:1~100:1; The method for preparing an aluminum/carbon composite that reacts with alkaline water to produce hydrogen according to claim 3, characterized in that: the diameter of the grinding ball used in the ball milling in step (2) is 5 mm-15 mm; The ball-to-material mass ratio of the grinding ball is 5:1~100:1;
    所述球磨的转速为100~2000转/分钟,球磨的时间为1分钟~50小时。The rotation speed of the ball mill is 100 to 2000 rpm, and the ball milling time is 1 minute to 50 hours.
  7. 根据权利要求3所述的与碱性水反应制氢的铝/碳复合物的制备方法,其特征在于:步骤(2)所述球磨的磨罐及磨球为玛瑙、氧化锆、硬质合金、聚氨酯或不锈钢;所述的保护气氛为氩气。 The method for preparing an aluminum/carbon composite that reacts with alkaline water to produce hydrogen according to claim 3, characterized in that: the grinding jar and the grinding ball of the ball mill in step (2) are agate, zirconia, cemented carbide , polyurethane or stainless steel; the protective atmosphere is argon.
  8. 权利要求1或2所述的与碱性水反应制氢的铝/碳复合物在与碱性水反应制氢中的应用。 Application of the aluminum/carbon composite that reacts with alkaline water to produce hydrogen according to claim 1 or 2 in reacting with alkaline water to produce hydrogen.
  9. 根据权利要求8所述的应用,其特征在于:所述碱性水中的碱为氢氧化钠、氢氧化钾、氢氧化钙或氢氧化锂中一种或多种的组合,碱的浓度为0.1~10 M; The application according to claim 8, characterized in that: the alkali in the alkaline water is one or more combinations of sodium hydroxide, potassium hydroxide, calcium hydroxide or lithium hydroxide, and the concentration of the alkali is 0.1 ~10M;
    所述铝/碳复合物和碱性水的重量比为1:5~1:1000。The weight ratio of the aluminum/carbon composite and alkaline water is 1:5~1:1000.
  10. 根据权利要求8所述的应用,其特征在于:制氢反应在室温环境中进行;制氢反应过程中不对体系温度进行控制。 The application according to claim 8, characterized in that: the hydrogen production reaction is carried out in a room temperature environment; the system temperature is not controlled during the hydrogen production reaction.
PCT/CN2022/128472 2022-06-28 2022-10-30 Aluminum/carbon composite for hydrogen production by means of reaction with alkaline water, and preparation method therefor and use thereof WO2024000963A1 (en)

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CN101463435A (en) * 2007-12-21 2009-06-24 成均馆大学校产学协力团 Encapsulation of carbon material within aluminum
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