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WO2020224431A1 - Aeolotropic layered carbon-fiber-based aerogel material and preparation method therefor - Google Patents

Aeolotropic layered carbon-fiber-based aerogel material and preparation method therefor Download PDF

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Publication number
WO2020224431A1
WO2020224431A1 PCT/CN2020/085989 CN2020085989W WO2020224431A1 WO 2020224431 A1 WO2020224431 A1 WO 2020224431A1 CN 2020085989 W CN2020085989 W CN 2020085989W WO 2020224431 A1 WO2020224431 A1 WO 2020224431A1
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Prior art keywords
chloride
carbon fiber
acid
based aerogel
fiber
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PCT/CN2020/085989
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French (fr)
Chinese (zh)
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伍晖
贾超
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清华大学
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Publication of WO2020224431A1 publication Critical patent/WO2020224431A1/en

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    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F9/00Artificial filaments or the like of other substances; Manufacture thereof; Apparatus specially adapted for the manufacture of carbon filaments
    • D01F9/08Artificial filaments or the like of other substances; Manufacture thereof; Apparatus specially adapted for the manufacture of carbon filaments of inorganic material
    • D01F9/12Carbon filaments; Apparatus specially adapted for the manufacture thereof
    • D01F9/14Carbon filaments; Apparatus specially adapted for the manufacture thereof by decomposition of organic filaments
    • D01F9/20Carbon filaments; Apparatus specially adapted for the manufacture thereof by decomposition of organic filaments from polyaddition, polycondensation or polymerisation products
    • D01F9/21Carbon filaments; Apparatus specially adapted for the manufacture thereof by decomposition of organic filaments from polyaddition, polycondensation or polymerisation products from macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F9/00Artificial filaments or the like of other substances; Manufacture thereof; Apparatus specially adapted for the manufacture of carbon filaments
    • D01F9/08Artificial filaments or the like of other substances; Manufacture thereof; Apparatus specially adapted for the manufacture of carbon filaments of inorganic material
    • D01F9/12Carbon filaments; Apparatus specially adapted for the manufacture thereof
    • D01F9/14Carbon filaments; Apparatus specially adapted for the manufacture thereof by decomposition of organic filaments
    • D01F9/20Carbon filaments; Apparatus specially adapted for the manufacture thereof by decomposition of organic filaments from polyaddition, polycondensation or polymerisation products
    • D01F9/24Carbon filaments; Apparatus specially adapted for the manufacture thereof by decomposition of organic filaments from polyaddition, polycondensation or polymerisation products from macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds

Definitions

  • the invention relates to the technical field of materials, in particular to an anisotropic layered carbon fiber-based aerogel material and a preparation method thereof.
  • Aerogel material is an ultra-light material with a three-dimensional network structure. Due to its ultra-low density, high specific surface area and porosity, and low thermal conductivity, it is used in heat insulation, sound absorption and noise reduction. , Catalyst carrier, air filtration and other fields show broad application prospects. Among them, in addition to the advantages of general aerogel materials, carbon aerogel materials also have the advantages of wide sources of raw materials and high electrical conductivity, so they have broad market prospects in the fields of energy storage, sensors, and electromagnetic shielding. At present, the preparation of fiber materials mainly adopts the electrostatic spinning method. Due to the direct spinning and deposition, the fibrous materials obtained by electrospinning are usually randomly stacked in the form of non-woven fabrics.
  • the fiber-based aerogel materials can be prepared by reasonable design of the receiving device, the real three-dimensional air with regular shapes is obtained. Gelation is still difficult.
  • the aerogel obtained by direct electrospinning has a disordered structure and therefore has poor compression resistance.
  • an object of the present invention is to provide a method for preparing an anisotropic layered carbon fiber-based aerogel material, which is simple, easy to operate, low in cost, and high in efficiency. Good flexibility, high compressibility or good conductivity.
  • the present invention provides a method for preparing an anisotropic layered carbon fiber-based aerogel material.
  • the method includes: mixing a polymer solution, an inorganic precursor, and a chloride to obtain a spinning precursor mixture; and performing jet spinning on the spinning precursor mixture to obtain a composite fiber Aerogel; the composite fiber aerogel is sequentially subjected to pre-oxidation treatment and carbonization treatment to obtain an anisotropic layered carbon fiber-based aerogel material.
  • the above-mentioned preparation method is simple, easy to operate, low-cost, high-efficiency, and easy for industrial production;
  • the carbon fiber-based aerogel material prepared by the above-mentioned method is composed of multi-layer stacked microfibers and has an anisotropic layered shape. The structure can be cut into any desired shape and stacked to the required thickness; and the prepared carbon fiber-based aerogel material has good flexibility and compressibility; the layered structure of the carbon fiber-based aerogel material
  • the carbon component makes aerogel materials have good electrical conductivity, and the electrical conductivity increases with the increase of compressive strain, which in turn makes it have broad application prospects in the fields of stress sensing, electromagnetic shielding, air filtration, energy storage and so on.
  • the polymer solution includes a polymer material and a solvent, wherein the mass ratio of the polymer material to the solvent is (2-30):100.
  • the spinning precursor mixture further includes a catalyst.
  • the spinning precursor mixture includes: 2-30 parts by weight of the polymer material; 100 parts by weight of the solvent; 0.5-100 parts by weight of the inorganic precursor; 0.001 -1 parts by weight of the catalyst; and 1-100 parts by weight of the chloride.
  • the polymer material is selected from polyvinyl alcohol, polyethylene glycol, polyurethane, polyacrylic acid, polyvinylpyrrolidone, cellulose acetate, methylcellulose, carboxymethylcellulose, polyvinylidene fluoride At least one of ethylene, polymethyl methacrylate, polyacrylamide, polyethylene oxide, polylactic acid, polyamide, polycaprolactone, polyvinyl butyral, polyaniline, polyimide, and polycarbonate Species
  • the solvent is selected from water, formic acid, tetrahydrofuran, acetone, butanone, n-hexane, cyclohexane, n-heptane, acetonitrile, N-methylpyrrolidone, 1,2-propanediol, chloroform, dichloromethane , 1,2-Dichloroethane, methanol, ethanol, isopropanol, tert-butanol, n-butanol, toluene, xylene, ethylenediamine, dimethyl sulfoxide, N,N-dimethylformamide , At least one of N,N-dimethylacetamide and carbon tetrachloride;
  • the inorganic precursor is at least one of zirconium oxychloride, zirconium acetate, aluminum isopropoxide, zirconium n-propoxide, ethyl orthosilicate, and methyl orthosilicate;
  • the catalyst is selected from at least one of phosphoric acid, sulfuric acid, hydrochloric acid, nitric acid, formic acid, acetic acid, hydrofluoric acid, perchloric acid, trifluoroacetic acid, citric acid, oxalic acid and maleic acid.
  • the chloride is selected from lithium chloride, sodium chloride, potassium chloride, rubidium chloride, cesium chloride, beryllium chloride, magnesium chloride, calcium chloride, strontium chloride, barium chloride , Radium chloride, zinc chloride, copper chloride, nickel chloride, cobalt chloride, ferric chloride, ferrous chloride, manganese chloride, chromium chloride, vanadium chloride, titanium tetrachloride, scandium chloride , Aluminum chloride, gallium chloride, indium chloride, thallium chloride, tin chloride, lead chloride, cadmium chloride, palladium chloride, rhodium chloride, ruthenium chloride, zirconium chloride, hafnium chloride, three At least one of osmium chloride, platinum chloride, gold chloride, and mercury chloride.
  • compressed air is used to eject the spinning precursor mixture from the nozzle of a jet spinning device.
  • the spinning precursor mixture is extruded
  • the speed is 0.1-15 ml/hour
  • the distance between the spinneret and the receiver is 20-100 cm
  • the air flow velocity of the compressed air is 1-50 m/sec.
  • the conditions of the pre-oxidation treatment and the carbonization treatment are respectively: in the air at a temperature increase rate of 0.5-10 °C/min to 180 °C ⁇ 300 °C, the pre-oxidation treatment 0.5 ⁇ 3 hours; in an inert gas atmosphere, the temperature is increased to 700°C to 1500°C at a temperature increase rate of 0.5 to 10°C/min, the carbonization treatment is performed for 0.5 to 3 hours, and then the temperature is lowered to room temperature.
  • the present invention provides an anisotropic layered carbon fiber-based aerogel material.
  • the anisotropic layered carbon fiber-based aerogel material is prepared by the aforementioned method.
  • the carbon fiber-based aerogel material is composed of multiple stacked microfibers and has an anisotropic layered structure, which can be cut into any desired shape and stacked to a desired thickness; moreover, the Carbon fiber-based aerogel materials have good flexibility and compressibility; the layered structure and carbon component of carbon fiber-based aerogel materials make carbon fiber-based aerogel materials have good electrical conductivity, and the conductivity varies with compression strain Increase and increase, and make it have broad application prospects in stress sensing, electromagnetic shielding, air filtration, energy storage and other fields.
  • the bulk density of the carbon fiber-based aerogel material is 5 to 200 mg/cm 3 , and optionally, the average diameter of the fibers in the carbon fiber-based aerogel material is 0.2 to 10 microns.
  • Fig. 1 is a flow chart of a preparation method of an anisotropic layered carbon fiber-based aerogel material in an embodiment of the present invention.
  • Fig. 2 is a scanning electron micrograph of an anisotropic layered carbon fiber-based aerogel material in another embodiment of the present invention.
  • the present invention provides a method for preparing an anisotropic layered carbon fiber-based aerogel material (referred to as carbon fiber-based aerogel material herein).
  • the preparation method of the anisotropic layered carbon fiber-based aerogel material includes:
  • the polymer solution includes a polymer material and a solvent, wherein the mass ratio of the polymer material to the solvent is (2-30): 100, such as 2: 100, 5: 100, 8: 100, 10 : 100, 15: 100, 20: 100, 25: 100, 30: 100.
  • a uniformly dissolved polymer solution can be obtained, and the polymer solution with the above concentration is conducive to subsequent jet spinning, and a carbon fiber-based aerogel material with excellent compressibility and flexibility can be obtained; if the polymer material is compatible with If the mass ratio of the solvent is less than 2:100, the concentration of the polymer solution is too low and fibers cannot be formed; if the mass ratio of the polymer material to the solvent is higher than 30:100, the polymer material is not easy to dissolve completely, and the second is high The viscosity of the molecular solution is too high to be ejected from the spinneret of the jet spinning equipment to form fibers.
  • the step of preparing the polymer solution includes: adding a certain amount of polymer material to a certain amount of solvent, and then at room temperature (25°C) to 100°C Under the conditions of stirring and dissolving at a speed of 50-1000 rpm for 0.1-10 hours, a polymer solution with a suitable concentration can be obtained.
  • the specific amount of polymer materials and solvents and specific process conditions can be determined by those skilled in the art according to specific The polymer material and the selected solvent are set. There are no restrictions here, as long as the polymer material is fully and quickly dissolved.
  • the stirring can be accomplished by mechanical stirring or magnetic stirring.
  • the polymer material is selected from polyvinyl alcohol, polyethylene glycol, polyurethane, polyacrylic acid, polyvinylpyrrolidone, cellulose acetate, methylcellulose, carboxymethylcellulose, polyvinylidene fluoride, At least one of polymethyl methacrylate, polyacrylamide, polyethylene oxide, polylactic acid, polyamide, polycaprolactone, polyvinyl butyral, polyaniline, polyimide, and polycarbonate. Therefore, the material source is wide, easy to spin, and it is convenient to carbonize the polymer material in the subsequent process.
  • the solvent is selected from water, formic acid, tetrahydrofuran, acetone, butanone, n-hexane, cyclohexane, n-heptane, acetonitrile, N-methylpyrrolidone, 1,2-propanediol, chloroform, dichloro Methane, 1,2-dichloroethane, methanol, ethanol, isopropanol, tert-butanol, n-butanol, toluene, xylene, ethylenediamine, dimethyl sulfoxide, N,N-dimethylformaldehyde At least one of amide, N,N-dimethylacetamide and carbon tetrachloride. Therefore, those skilled in the art can choose suitable solvents according to different polymer materials to ensure that the polymer materials can be quickly and effectively dissolved.
  • the inorganic precursor is at least one of zirconium oxychloride, zirconium acetate, aluminum isopropoxide, zirconium n-propoxide, ethyl orthosilicate, and methyl orthosilicate.
  • the above-mentioned inorganic precursors are hydrolyzed to obtain oxides (such as zirconia, alumina, and silica), and composite fiber aerogel materials are obtained by jet spinning.
  • the chloride is selected from lithium chloride, sodium chloride, potassium chloride, rubidium chloride, cesium chloride, beryllium chloride, magnesium chloride, Calcium chloride, strontium chloride, barium chloride, radium chloride, zinc chloride, copper chloride, nickel chloride, cobalt chloride, ferric chloride, ferrous chloride, manganese chloride, chromium chloride, chlorine Vanadium chloride, titanium tetrachloride, scandium chloride, aluminum chloride, gallium chloride, indium chloride, thallium chloride, tin chloride, lead chloride, cadmium chloride, palladium chloride, rhodium chloride, chloride At least one of ruthenium, zirconium chloride, hafnium chloride, osmium chloride, platinum chloride, gold chloride, and mercury chloride. Therefore, in the process of jet
  • a catalyst is further included in the spinning precursor mixture.
  • the catalyst is selected from at least one of phosphoric acid, sulfuric acid, hydrochloric acid, nitric acid, formic acid, acetic acid, hydrofluoric acid, perchloric acid, trifluoroacetic acid, citric acid, oxalic acid and maleic acid . Therefore, under the action of the above-mentioned catalyst, the inorganic precursor can be hydrolyzed into inorganic oxides quickly, effectively and more fully to obtain composite fiber aerogel materials, which is beneficial for subsequent production of carbon fiber-based aerogel materials with excellent performance. .
  • the inorganic precursor, catalyst and chloride are added to the polymer solution separately, and a spinning precursor mixture with a certain viscosity is obtained by stirring; in other embodiments of the present invention, The inorganic precursor, catalyst and chloride are mixed first, and then added to the polymer solution, and a spinning precursor mixture with a certain viscosity is obtained by stirring.
  • the specific method of stirring is also not limited. It can be mechanical stirring or magnetic stirring, which is not limited here.
  • the spinning precursor mixture includes: 2-30 parts by weight of polymer material; 100 parts by weight of solvent; 0.5-100 parts by weight Inorganic precursor; 0.001 to 1 parts by weight of catalyst; and 1 to 100 parts by weight of chloride. Therefore, the carbon fiber-based aerogel material prepared by the above ratio has good compressibility, flexibility, and an anisotropic layered structure, wherein the amount of chloride can effectively ensure the layered shape of the carbon fiber-based aerogel structure. If the amount of chloride is too low, the layered structure of the carbon fiber-based aerogel material is not obvious, resulting in relatively poor compressibility; if the amount of chloride is too high, it will also cause the compressibility of the aerogel material Getting worse.
  • anisotropy means that the carbon fiber-based aerogel material is compressed from different directions relative to the carbon fiber layer in the carbon fiber-based aerogel material, and its compressibility is different, and the recovery performance is different, such as compression from a direction perpendicular to the carbon fiber layer
  • Carbon fiber-based aerogel materials carbon fiber-based aerogel materials can be completely restored to their original state, while compressing carbon fiber-based aerogel materials from a direction parallel to the carbon fiber layer, carbon fiber-based aerogel materials cannot be restored to their original state.
  • the spinning precursor mixture is spun using the jet spinning technology, and the spinning precursor mixture is ejected from the spinneret of the jet spinning equipment by compressed air, specifically: Jet spinning adopts a pair of coaxial nozzles, using compressed air to extrude the spinning precursor mixture through the inner nozzle, and the high-speed airflow is ejected through the outer nozzle.
  • the spinning precursor mixture is polymerized under the shearing action of the high-speed airflow.
  • the jet further splits, stretches, and refines.
  • the solvent continuously volatilizes, and the fibers are formed and solidified and collected on the receiving device (also called "receiver").
  • the jet spinning equipment is simple, uses high-speed airflow as the driving force, does not require high-voltage electrostatic field, has higher spinning efficiency, and the composite fiber aerogel can be deposited on any substrate. Therefore, it is of great significance to use jet spinning technology to prepare large-scale carbon fiber-based aerogel materials with good flexibility and conductivity.
  • the receiving device includes but is not limited to metal mesh, plastic mesh, and non-woven fabric.
  • the extrusion speed of the spinning precursor mixture is 0.1-15 ml/h (E.g. 0.1mL/h, 0.5mL/h, 1mL/h, 2mL/h, 3mL/h, 4mL/h, 5mL/h, 6mL/h, 7mL/h, 8mL/h, 9mL/h, 10mL/ h, 11mL/h, 12mL/h, 13mL/h, 14mL/h, 15mL/h), the distance between the spinneret and the receiver is 20-100 cm (such as 20cm, 30cm, 40cm, 50cm, 60cm, 70cm, 80cm, 90cm, 100cm), the compressed air flow velocity is 1-50m/s (such as 1m/s, 5m/s, 10m/s, 15m/s, 20m/s
  • S300 Perform pre-oxidation treatment and carbonization treatment on the composite fiber aerogel in sequence to obtain an anisotropic layered carbon fiber-based aerogel material.
  • the polymer material is pyrolyzed, and the elements such as hydrogen and oxygen are removed to form carbon fibers.
  • the carbon fiber-based aerogel material is obtained, making the layered structure of the carbon fiber-based aerogel material excellent The conductivity.
  • the conditions of the pre-oxidation treatment and the carbonization treatment are respectively: 0.5-10°C/min (such as 0.5°C/min, 1°C/min) in the air , 2°C/min, 3°C/min, 4°C/min, 5°C/min, 6°C/min, 7°C/min, 8°C/min, 9°C/min, 10°C/min)
  • 0.5-10°C/min such as 0.5°C/min, 1°C/min
  • 180°C ⁇ 300°C such as 180°C, 200°C, 230°C, 250°C, 280°C or 300°C
  • pre-oxidation treatment for 0.5 ⁇ 3 hours (such as 0.5 hour, 1 hour, 1.5 hours, 2 hours, 2.5 Hours or 3 hours);
  • 0.5 ⁇ 10°C/min such as 0.5°C/min, 1°C/min, 2°C/min, 3°C/min, 4°C/min, 5°C/min
  • the preparation method of the above-mentioned carbon fiber-based aerogel material is simple, easy to operate, low-cost, high-efficiency, and easy for industrial production;
  • the carbon-fiber-based aerogel material prepared by the above method is stacked by multiple layers It is composed of microfibers and has an anisotropic layered structure, which can be cut into any desired shape and stacked to a desired thickness; and the prepared carbon fiber-based aerogel material has good flexibility and compressibility;
  • the layered structure and carbon component of carbon fiber-based aerogel materials make the aerogel materials have good electrical conductivity, and the electrical conductivity increases with the increase of compressive strain, which in turn makes it useful for stress sensing, electromagnetic shielding, and air filtration. , Energy storage and other fields have broad application prospects.
  • the present invention provides an anisotropic layered carbon fiber-based aerogel material.
  • the anisotropic layered carbon fiber-based aerogel material is prepared by the aforementioned method.
  • the carbon fiber-based aerogel material is composed of multiple stacked microfibers and has an anisotropic layered structure, which can be cut into any desired shape and stacked to a desired thickness; moreover, the Carbon fiber-based aerogel materials have good flexibility and compressibility; the layered structure and carbon component of carbon fiber-based aerogel materials make the aerogel materials have good electrical conductivity, and the electrical conductivity increases with the increase in compression strain. Increase, and make it have broad application prospects in stress sensing, electromagnetic shielding, air filtration, energy storage and other fields.
  • the bulk density of the carbon fiber-based aerogel material is 5 to 200 mg/cm 3 (such as 5 mg/cm 3 , 25 mg/cm 3 , 50 mg/cm 3 , 75 mg/cm 3 , 100 mg/cm 3 , 125mg/cm 3 , 150mg/cm 3 , 175mg/cm 3 , 200mg/cm 3 , ), the average diameter of the fibers in the carbon fiber-based aerogel material is 0.2-10 microns (such as 0.2 microns, 0.5 microns, 1 microns, 2 Microns, 4 microns, 6 microns, 8 microns or 10 microns).
  • the bulk density and fiber diameter of carbon fiber-based aerogel materials have a wide range.
  • Those skilled in the art can prepare carbon fiber-based aerogel materials with different bulk densities and fiber diameters according to different needs and applications to meet different requirements. Market demand.
  • a preparation method of anisotropic layered carbon fiber-based aerogel material adopts the following process steps:
  • Jet spinning using jet spinning technology to use compressed air with a flow rate of 5m/s to eject the spinning precursor mixture from the spinneret at a speed of 5mL/h, and the resulting fiber is deposited at a distance from the spinneret Obtain composite fiber aerogel on a 60cm metal mesh receiver;
  • the obtained anisotropic layered carbon fiber-based aerogel material has a bulk density of 20 mg/cm 3 and an average fiber diameter of 3.3 ⁇ m. Refer to FIG. 2 for the scanning electron microscope image.
  • a preparation method of anisotropic layered carbon fiber-based aerogel material adopts the following process steps:
  • Jet spinning using jet spinning technology to use compressed air with a flow rate of 5m/s to eject the spinning precursor mixture from the spinneret at a speed of 5mL/h, and the resulting fiber is deposited at a distance from the spinneret Obtain composite fiber aerogel on a 60cm metal mesh receiver;
  • the resulting product has an anisotropic layered carbon fiber-based aerogel material with a bulk density of 19 mg/cm 3 and an average fiber diameter of 3.6 ⁇ m.
  • a preparation method of anisotropic layered carbon fiber-based aerogel material adopts the following process steps:
  • Jet spinning using jet spinning technology to use compressed air with a flow rate of 5m/s to eject the spinning precursor mixture from the spinneret at a speed of 5mL/h, and the resulting fiber is deposited at a distance from the spinneret Obtain composite fiber aerogel on a 60cm metal mesh receiver;
  • Pre-oxidation and carbonization The obtained composite fiber aerogel is heated at 1.5°C/min to 300°C for 1h in an air atmosphere, and then heated at 5°C/min to 900°C in a nitrogen atmosphere. The carbonization treatment was carried out for 2 hours, and the anisotropic layered carbon fiber-based aerogel material was obtained after being cooled to room temperature.
  • the resulting product has an anisotropic layered carbon fiber-based aerogel material with a bulk density of 17 mg/cm 3 and an average fiber diameter of 3.9 ⁇ m.
  • a preparation method of anisotropic layered carbon fiber-based aerogel material adopts the following process steps:
  • Jet spinning using jet spinning technology to use compressed air with a flow rate of 5m/s to eject the spinning precursor mixture from the spinneret at a speed of 5mL/h, and the resulting fiber is deposited at a distance from the spinneret Obtain composite fiber aerogel on a 60cm metal mesh receiver;
  • the resulting product has an anisotropic layered carbon fiber-based aerogel material with a bulk density of 22 mg/cm 3 and an average fiber diameter of 3.6 ⁇ m.
  • a preparation method of anisotropic layered carbon fiber-based aerogel material adopts the following process steps:
  • Jet spinning using solution jet spinning technology to use compressed air with a flow rate of 5m/s to eject the spinning precursor mixture from the spinneret at a speed of 5mL/h, and the resulting fibers are deposited in the distance spinning
  • the composite fiber aerogel is obtained on the metal mesh receiver with an opening of 60 cm;
  • Pre-oxidation and carbonization The obtained composite fiber aerogel is heated at 1°C/min to 300°C for 2h in an air atmosphere, and then heated at 5°C/min to 900°C in a nitrogen atmosphere. The carbonization treatment was carried out for 2 hours, and the anisotropic layered carbon fiber-based aerogel material was obtained after being cooled to room temperature.
  • the resulting product has an anisotropic layered carbon fiber-based aerogel material with a bulk density of 21 mg/cm 3 and an average fiber diameter of 4.3 ⁇ m.

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Abstract

Provided are an aeolotropic layered carbon-fiber-based aerogel material and a preparation method therefor. The method for preparing the aeolotropic layered carbon-fiber-based aerogel material comprises: mixing a polymer solution, an inorganic precursor and a chloride to obtain a spinning precursor mixed liquid; jet spinning the spinning precursor mixed liquid to obtain a composite fiber aerogel; and subjecting the composite fiber aerogel to pre-oxidation and carbonization treatments successively, to obtain the aeolotropic layered carbon-fiber-based aerogel material. Thus, the preparation method is simple, easy to operate, low in preparation cost, high in efficiency, and easy for industrial production. The carbon-fiber-based aerogel material prepared by the method is composed of multiple layers of stacked microfibers, has an aeolotropic layered structure, and can be cut into any desired shape and stacked into a desired thickness; moreover, the material has good flexibility, compressibility and electrical conductivity.

Description

一种各向异性层状碳纤维基气凝胶材料及其制备方法Anisotropic layered carbon fiber-based aerogel material and preparation method thereof
优先权信息Priority information
本申请请求2019年05月07日向中国国家知识产权局提交的、专利申请号为201910375720.9的专利申请的优先权和权益,并且通过参照将其全文并入此处。This application requests the priority and rights of the patent application with the patent application number 201910375720.9 filed with the State Intellectual Property Office of China on May 7, 2019, and the full text is incorporated herein by reference.
技术领域Technical field
本发明涉及材料技术领域,具体的,涉及一种各向异性层状碳纤维基气凝胶材料及其制备方法。The invention relates to the technical field of materials, in particular to an anisotropic layered carbon fiber-based aerogel material and a preparation method thereof.
背景技术Background technique
气凝胶材料是一种具有三维网络结构的超轻材料,由于其具有超低的密度、高的比表面积和孔隙率、较低的热导率等优点,因而在隔热保温、吸音降噪、催化剂载体、空气过滤等领域表现出广阔的应用前景。其中,碳气凝胶材料除了具有一般气凝胶材料的优点外,还具有原料来源广泛、电导率高等优点,因而在能源存储、传感器、电磁屏蔽等领域具有广阔的市场前景。当前,制备纤维材料主要采用静电纺丝法。由于直接纺丝沉积的原因,静电纺丝得到的纤维材料通常随机堆积成无纺布形式,尽管通过合理设计接收装置可以制备得到纤维基气凝胶材料,但获得具有规则形状的真正的三维气凝胶仍然很困难。此外,直接静电纺丝得到的气凝胶具有无序的结构,因而抗压缩性能很差。Aerogel material is an ultra-light material with a three-dimensional network structure. Due to its ultra-low density, high specific surface area and porosity, and low thermal conductivity, it is used in heat insulation, sound absorption and noise reduction. , Catalyst carrier, air filtration and other fields show broad application prospects. Among them, in addition to the advantages of general aerogel materials, carbon aerogel materials also have the advantages of wide sources of raw materials and high electrical conductivity, so they have broad market prospects in the fields of energy storage, sensors, and electromagnetic shielding. At present, the preparation of fiber materials mainly adopts the electrostatic spinning method. Due to the direct spinning and deposition, the fibrous materials obtained by electrospinning are usually randomly stacked in the form of non-woven fabrics. Although the fiber-based aerogel materials can be prepared by reasonable design of the receiving device, the real three-dimensional air with regular shapes is obtained. Gelation is still difficult. In addition, the aerogel obtained by direct electrospinning has a disordered structure and therefore has poor compression resistance.
因此,关于碳纤维基气凝胶材料的制备方法有待深入研究。Therefore, the preparation method of carbon fiber-based aerogel materials needs further research.
发明内容Summary of the invention
本发明旨在至少在一定程度上解决相关技术中的技术问题之一。为此,本发明的一个目的在于提出一种各向异性层状碳纤维基气凝胶材料的制备方法,该方法简单、易操作,制备成本低,效率高,制备的碳纤维基气凝胶材料的柔韧性好、可压缩性高或导电性佳。The present invention aims to solve one of the technical problems in the related art at least to a certain extent. To this end, an object of the present invention is to provide a method for preparing an anisotropic layered carbon fiber-based aerogel material, which is simple, easy to operate, low in cost, and high in efficiency. Good flexibility, high compressibility or good conductivity.
在本发明的一个方面,本发明提供了一种各向异性层状碳纤维基气凝胶材料的制备方法。根据本发明的实施例,所述方法包括:将高分子溶液、无机前驱体和氯化物混合,得到纺丝前驱体混合液;对所述纺丝前驱体混合液进行喷射纺丝,得到复合纤维气凝胶;对所述复合纤维气凝胶依次进行预氧化处理和碳化处理,得到各向异性层 状碳纤维基气凝胶材料。由此,上述制备方法简单,易操作,制备成本低、效率高,易于工业化生产;由上述方法制备的碳纤维基气凝胶材料是由多层堆叠的微纤维构成,具有各向异性的层状结构,可以裁切成所需的任意形状,以及堆叠成所需的厚度;而且制备的碳纤维基气凝胶材料具有良好的柔韧性和可压缩性;碳纤维基气凝胶材料的层状结构和碳组分使得气凝胶材料具有良好的导电性,并且电导率随压缩应变的增加而增大,进而使其在应力传感、电磁屏蔽、空气过滤、能源存储等领域有着广阔的应用前景。In one aspect of the present invention, the present invention provides a method for preparing an anisotropic layered carbon fiber-based aerogel material. According to an embodiment of the present invention, the method includes: mixing a polymer solution, an inorganic precursor, and a chloride to obtain a spinning precursor mixture; and performing jet spinning on the spinning precursor mixture to obtain a composite fiber Aerogel; the composite fiber aerogel is sequentially subjected to pre-oxidation treatment and carbonization treatment to obtain an anisotropic layered carbon fiber-based aerogel material. Therefore, the above-mentioned preparation method is simple, easy to operate, low-cost, high-efficiency, and easy for industrial production; the carbon fiber-based aerogel material prepared by the above-mentioned method is composed of multi-layer stacked microfibers and has an anisotropic layered shape. The structure can be cut into any desired shape and stacked to the required thickness; and the prepared carbon fiber-based aerogel material has good flexibility and compressibility; the layered structure of the carbon fiber-based aerogel material The carbon component makes aerogel materials have good electrical conductivity, and the electrical conductivity increases with the increase of compressive strain, which in turn makes it have broad application prospects in the fields of stress sensing, electromagnetic shielding, air filtration, energy storage and so on.
根据本发明的实施例,所述高分子溶液包括高分子材料和溶剂,其中,所述高分子材料与所述溶剂的质量比为(2~30):100。According to an embodiment of the present invention, the polymer solution includes a polymer material and a solvent, wherein the mass ratio of the polymer material to the solvent is (2-30):100.
根据本发明的实施例,所述纺丝前驱体混合液中进一步包括催化剂。According to an embodiment of the present invention, the spinning precursor mixture further includes a catalyst.
根据本发明的实施例,所述纺丝前驱体混合液包括:2~30重量份的所述高分子材料;100重量份的所述溶剂;0.5~100重量份的所述无机前驱体;0.001~1重量份的所述催化剂;及1~100重量份的所述氯化物。According to an embodiment of the present invention, the spinning precursor mixture includes: 2-30 parts by weight of the polymer material; 100 parts by weight of the solvent; 0.5-100 parts by weight of the inorganic precursor; 0.001 -1 parts by weight of the catalyst; and 1-100 parts by weight of the chloride.
根据本发明的实施例,所述高分子材料选自聚乙烯醇、聚乙二醇、聚氨酯、聚丙烯酸、聚乙烯吡咯烷酮、醋酸纤维素、甲基纤维素、羧甲基纤维素、聚偏氟乙烯、聚甲基丙烯酸甲酯、聚丙烯酰胺、聚氧化乙烯、聚乳酸、聚酰胺、聚己内酯、聚乙烯醇缩丁醛、聚苯胺、聚酰亚胺和聚碳酸酯中的至少一种;According to an embodiment of the present invention, the polymer material is selected from polyvinyl alcohol, polyethylene glycol, polyurethane, polyacrylic acid, polyvinylpyrrolidone, cellulose acetate, methylcellulose, carboxymethylcellulose, polyvinylidene fluoride At least one of ethylene, polymethyl methacrylate, polyacrylamide, polyethylene oxide, polylactic acid, polyamide, polycaprolactone, polyvinyl butyral, polyaniline, polyimide, and polycarbonate Species
任选地,所述溶剂选自水、甲酸、四氢呋喃、丙酮、丁酮、正己烷、环己烷、正庚烷、乙腈、N-甲基吡咯烷酮、1,2-丙二醇、氯仿、二氯甲烷、1,2-二氯乙烷、甲醇、乙醇、异丙醇、叔丁醇、正丁醇、甲苯、二甲苯、乙二胺、二甲基亚砜、N,N-二甲基甲酰胺、N,N-二甲基乙酰胺和四氯化碳中的至少一种;Optionally, the solvent is selected from water, formic acid, tetrahydrofuran, acetone, butanone, n-hexane, cyclohexane, n-heptane, acetonitrile, N-methylpyrrolidone, 1,2-propanediol, chloroform, dichloromethane , 1,2-Dichloroethane, methanol, ethanol, isopropanol, tert-butanol, n-butanol, toluene, xylene, ethylenediamine, dimethyl sulfoxide, N,N-dimethylformamide , At least one of N,N-dimethylacetamide and carbon tetrachloride;
任选地,所述无机前驱体为氧氯化锆、乙酸锆、异丙醇铝、正丙醇锆、正硅酸乙酯和正硅酸甲酯中的至少一种;Optionally, the inorganic precursor is at least one of zirconium oxychloride, zirconium acetate, aluminum isopropoxide, zirconium n-propoxide, ethyl orthosilicate, and methyl orthosilicate;
任选地,所述催化剂选自磷酸、硫酸、盐酸、硝酸、甲酸、醋酸、氢氟酸、高氯酸、三氟乙酸、柠檬酸、草酸和马来酸中的至少一种。Optionally, the catalyst is selected from at least one of phosphoric acid, sulfuric acid, hydrochloric acid, nitric acid, formic acid, acetic acid, hydrofluoric acid, perchloric acid, trifluoroacetic acid, citric acid, oxalic acid and maleic acid.
根据本发明的实施例,所述氯化物选自氯化锂、氯化钠、氯化钾、氯化铷、氯化铯、氯化铍、氯化镁、氯化钙、氯化锶、氯化钡、氯化镭、氯化锌、氯化铜、氯化镍、氯化钴、氯化铁、氯化亚铁、氯化锰、氯化铬、氯化钒、四氯化钛、氯化钪、氯化铝、氯化镓、氯化铟、氯化铊、氯化锡、氯化铅、氯化镉、氯化钯、氯化铑、氯化钌、氯化锆、氯化铪、三氯化锇、氯化铂、氯化金和氯化汞中的至少一种。According to an embodiment of the present invention, the chloride is selected from lithium chloride, sodium chloride, potassium chloride, rubidium chloride, cesium chloride, beryllium chloride, magnesium chloride, calcium chloride, strontium chloride, barium chloride , Radium chloride, zinc chloride, copper chloride, nickel chloride, cobalt chloride, ferric chloride, ferrous chloride, manganese chloride, chromium chloride, vanadium chloride, titanium tetrachloride, scandium chloride , Aluminum chloride, gallium chloride, indium chloride, thallium chloride, tin chloride, lead chloride, cadmium chloride, palladium chloride, rhodium chloride, ruthenium chloride, zirconium chloride, hafnium chloride, three At least one of osmium chloride, platinum chloride, gold chloride, and mercury chloride.
根据本发明的实施例,利用压缩空气将所述纺丝前驱体混合液从喷射纺丝设备的喷丝口喷出,在所述喷射纺丝中,所述纺丝前驱体混合液的挤出速度为0.1~15毫升/小时,所述喷丝口与所述接收器之间的距离为20~100厘米,所述压缩空气的气流流速为1~50米/秒。According to an embodiment of the present invention, compressed air is used to eject the spinning precursor mixture from the nozzle of a jet spinning device. In the jet spinning, the spinning precursor mixture is extruded The speed is 0.1-15 ml/hour, the distance between the spinneret and the receiver is 20-100 cm, and the air flow velocity of the compressed air is 1-50 m/sec.
根据本发明的实施例,所述预氧化处理和所述碳化处理的条件分别为:在空气中以0.5~10℃/min的升温速度升至180℃~300℃,进行所述预氧化处理0.5~3小时;在惰性气体氛围中,以0.5~10℃/min的升温速度升至700℃~1500℃,进行所述碳化处理0.5~3小时,之后降温至室温。According to an embodiment of the present invention, the conditions of the pre-oxidation treatment and the carbonization treatment are respectively: in the air at a temperature increase rate of 0.5-10 ℃/min to 180 ℃ ~ 300 ℃, the pre-oxidation treatment 0.5 ~3 hours; in an inert gas atmosphere, the temperature is increased to 700°C to 1500°C at a temperature increase rate of 0.5 to 10°C/min, the carbonization treatment is performed for 0.5 to 3 hours, and then the temperature is lowered to room temperature.
在本发明的又一方面,本发明提供了一种各向异性层状碳纤维基气凝胶材料。根据本发明的实施例,所述各向异性层状碳纤维基气凝胶材料是由前面所述的方法制备得到的。由此,该碳纤维基气凝胶材料是由多层堆叠的微纤维构成,具有各向异性的层状结构,可以裁切成所需的任意形状,以及堆叠成所需的厚度;而且,该碳纤维基气凝胶材料具有良好的柔韧性和可压缩性;碳纤维基气凝胶材料的层状结构和碳组分使得碳纤维基气凝胶材料具有良好的导电性,并且电导率随压缩应变的增加而增大,进而使其在应力传感、电磁屏蔽、空气过滤、能源存储等领域有着广阔的应用前景。In another aspect of the present invention, the present invention provides an anisotropic layered carbon fiber-based aerogel material. According to an embodiment of the present invention, the anisotropic layered carbon fiber-based aerogel material is prepared by the aforementioned method. Thus, the carbon fiber-based aerogel material is composed of multiple stacked microfibers and has an anisotropic layered structure, which can be cut into any desired shape and stacked to a desired thickness; moreover, the Carbon fiber-based aerogel materials have good flexibility and compressibility; the layered structure and carbon component of carbon fiber-based aerogel materials make carbon fiber-based aerogel materials have good electrical conductivity, and the conductivity varies with compression strain Increase and increase, and make it have broad application prospects in stress sensing, electromagnetic shielding, air filtration, energy storage and other fields.
根据本发明的实施例,所述碳纤维基气凝胶材料的体积密度为5~200mg/cm 3,任选地,所述碳纤维基气凝胶材料中纤维的平均直径为0.2~10微米。 According to an embodiment of the present invention, the bulk density of the carbon fiber-based aerogel material is 5 to 200 mg/cm 3 , and optionally, the average diameter of the fibers in the carbon fiber-based aerogel material is 0.2 to 10 microns.
附图说明Description of the drawings
图1是本发明一个实施例中各向异性层状碳纤维基气凝胶材料的制备方法流程图。Fig. 1 is a flow chart of a preparation method of an anisotropic layered carbon fiber-based aerogel material in an embodiment of the present invention.
图2是本发明又一个实施例中各向异性层状碳纤维基气凝胶材料的扫描电镜图。Fig. 2 is a scanning electron micrograph of an anisotropic layered carbon fiber-based aerogel material in another embodiment of the present invention.
发明详细描述Detailed description of the invention
下面详细描述本发明的实施例。下面描述的实施例是示例性的,仅用于解释本发明,而不能理解为对本发明的限制。实施例中未注明具体技术或条件的,按照本领域内的文献所描述的技术或条件或者按照产品说明书进行。所用试剂或仪器未注明生产厂商者,均为可以通过市购获得的常规产品。The embodiments of the present invention are described in detail below. The embodiments described below are exemplary, and are only used to explain the present invention, but should not be construed as limiting the present invention. Where specific techniques or conditions are not indicated in the examples, the procedures shall be carried out in accordance with the techniques or conditions described in the literature in the field or in accordance with the product specification. The reagents or instruments used without the manufacturer's indication are all conventional products that are commercially available.
在本发明的一个方面,本发明提供了一种各向异性层状碳纤维基气凝胶材料(本文中可简称碳纤维基气凝胶材料)的制备方法。根据本发明的实施例,参照图1,所述各向异性层状碳纤维基气凝胶材料的制备方法包括:In one aspect of the present invention, the present invention provides a method for preparing an anisotropic layered carbon fiber-based aerogel material (referred to as carbon fiber-based aerogel material herein). According to an embodiment of the present invention, referring to FIG. 1, the preparation method of the anisotropic layered carbon fiber-based aerogel material includes:
S100:将高分子溶液、无机前驱体和氯化物混合,得到纺丝前驱体混合液。在该过程中,无机前驱体发生水解,得到无机氧化物,以便后续得到碳纤维基气凝胶材料。S100: Mixing the polymer solution, the inorganic precursor and the chloride to obtain a spinning precursor mixture. In this process, the inorganic precursors are hydrolyzed to obtain inorganic oxides so as to subsequently obtain carbon fiber-based aerogel materials.
根据本发明的实施例,高分子溶液包括高分子材料和溶剂,其中,高分子材料与溶剂的质量比为(2~30):100,比如2:100、5:100、8:100、10:100、15:100、20:100、25:100、30:100。由此,可以得到溶解均匀的高分子溶液,而且上述浓度的高分子溶液有利于后续的喷射纺丝,得到可压缩性、柔韧性等性能优异的碳纤维基气凝胶材料;若高分子材料与溶剂的质量比低于2:100,则高分子溶液浓度过低,无法形成纤维;若高分子材料与溶剂的质量比高于30:100,一则高分子材料不易于全部溶解,二则高分子溶液粘度过高,难以从喷射纺丝设备的喷丝口喷出形成纤维。According to an embodiment of the present invention, the polymer solution includes a polymer material and a solvent, wherein the mass ratio of the polymer material to the solvent is (2-30): 100, such as 2: 100, 5: 100, 8: 100, 10 : 100, 15: 100, 20: 100, 25: 100, 30: 100. As a result, a uniformly dissolved polymer solution can be obtained, and the polymer solution with the above concentration is conducive to subsequent jet spinning, and a carbon fiber-based aerogel material with excellent compressibility and flexibility can be obtained; if the polymer material is compatible with If the mass ratio of the solvent is less than 2:100, the concentration of the polymer solution is too low and fibers cannot be formed; if the mass ratio of the polymer material to the solvent is higher than 30:100, the polymer material is not easy to dissolve completely, and the second is high The viscosity of the molecular solution is too high to be ejected from the spinneret of the jet spinning equipment to form fibers.
根据本发明的实施例,为了得到充分溶解的高分子溶液,配制高分子溶液的步骤包括:将一定量的高分子材料添加到一定量的溶剂中,之后在室温(25℃)~100℃的条件下以50~1000rpm的转速下搅拌溶解0.1~10小时,即可得到浓度适宜的高分子溶液,其中,高分子材料和溶剂的具体用量以及具体的工艺条件,本领域技术人员可以根据具体的高分子材料和选择的溶剂进行设定,在此不作限制要求,只要保证高分子材料充分快速的溶解即可。其中,搅拌可以通过机械搅拌或磁力搅拌完成。According to an embodiment of the present invention, in order to obtain a fully dissolved polymer solution, the step of preparing the polymer solution includes: adding a certain amount of polymer material to a certain amount of solvent, and then at room temperature (25°C) to 100°C Under the conditions of stirring and dissolving at a speed of 50-1000 rpm for 0.1-10 hours, a polymer solution with a suitable concentration can be obtained. Among them, the specific amount of polymer materials and solvents and specific process conditions can be determined by those skilled in the art according to specific The polymer material and the selected solvent are set. There are no restrictions here, as long as the polymer material is fully and quickly dissolved. Among them, the stirring can be accomplished by mechanical stirring or magnetic stirring.
根据本发明的实施例,高分子材料选自聚乙烯醇、聚乙二醇、聚氨酯、聚丙烯酸、聚乙烯吡咯烷酮、醋酸纤维素、甲基纤维素、羧甲基纤维素、聚偏氟乙烯、聚甲基丙烯酸甲酯、聚丙烯酰胺、聚氧化乙烯、聚乳酸、聚酰胺、聚己内酯、聚乙烯醇缩丁醛、聚苯胺、聚酰亚胺和聚碳酸酯中的至少一种。由此,材料来源广泛,易于纺丝,而且便于在后续将高分子材料碳化处理。According to an embodiment of the present invention, the polymer material is selected from polyvinyl alcohol, polyethylene glycol, polyurethane, polyacrylic acid, polyvinylpyrrolidone, cellulose acetate, methylcellulose, carboxymethylcellulose, polyvinylidene fluoride, At least one of polymethyl methacrylate, polyacrylamide, polyethylene oxide, polylactic acid, polyamide, polycaprolactone, polyvinyl butyral, polyaniline, polyimide, and polycarbonate. Therefore, the material source is wide, easy to spin, and it is convenient to carbonize the polymer material in the subsequent process.
根据本发明的实施例,溶剂选自水、甲酸、四氢呋喃、丙酮、丁酮、正己烷、环己烷、正庚烷、乙腈、N-甲基吡咯烷酮、1,2-丙二醇、氯仿、二氯甲烷、1,2-二氯乙烷、甲醇、乙醇、异丙醇、叔丁醇、正丁醇、甲苯、二甲苯、乙二胺、二甲基亚砜、N,N-二甲基甲酰胺、N,N-二甲基乙酰胺和四氯化碳中的至少一种。由此,本领域技术人员可以根据不同的高分子材料选择适宜的溶剂,保证高分子材料可以快速有效地被溶解掉。According to an embodiment of the present invention, the solvent is selected from water, formic acid, tetrahydrofuran, acetone, butanone, n-hexane, cyclohexane, n-heptane, acetonitrile, N-methylpyrrolidone, 1,2-propanediol, chloroform, dichloro Methane, 1,2-dichloroethane, methanol, ethanol, isopropanol, tert-butanol, n-butanol, toluene, xylene, ethylenediamine, dimethyl sulfoxide, N,N-dimethylformaldehyde At least one of amide, N,N-dimethylacetamide and carbon tetrachloride. Therefore, those skilled in the art can choose suitable solvents according to different polymer materials to ensure that the polymer materials can be quickly and effectively dissolved.
根据本发明的实施例,无机前驱体为氧氯化锆、乙酸锆、异丙醇铝、正丙醇锆、正硅酸乙酯和正硅酸甲酯中的至少一种。由此,上述无机前驱体在水解后得到氧化物(比如氧化锆、氧化铝、二氧化硅),通过喷射纺丝得到复合纤维气凝胶材料。According to an embodiment of the present invention, the inorganic precursor is at least one of zirconium oxychloride, zirconium acetate, aluminum isopropoxide, zirconium n-propoxide, ethyl orthosilicate, and methyl orthosilicate. Thus, the above-mentioned inorganic precursors are hydrolyzed to obtain oxides (such as zirconia, alumina, and silica), and composite fiber aerogel materials are obtained by jet spinning.
根据本发明的实施例,为了得到层状结构的碳纤维基气凝胶材料,氯化物选自氯化锂、氯化钠、氯化钾、氯化铷、氯化铯、氯化铍、氯化镁、氯化钙、氯化锶、氯化钡、氯化镭、 氯化锌、氯化铜、氯化镍、氯化钴、氯化铁、氯化亚铁、氯化锰、氯化铬、氯化钒、四氯化钛、氯化钪、氯化铝、氯化镓、氯化铟、氯化铊、氯化锡、氯化铅、氯化镉、氯化钯、氯化铑、氯化钌、氯化锆、氯化铪、三氯化锇、氯化铂、氯化金和氯化汞中的至少一种。由此,在喷射纺丝的过程中,在氯化物的作用下,可以得到层状结构的复合纤维气凝胶材料,从而大大提高碳纤维基气凝胶材料的可压缩性能。According to an embodiment of the present invention, in order to obtain a layered structure of carbon fiber-based aerogel material, the chloride is selected from lithium chloride, sodium chloride, potassium chloride, rubidium chloride, cesium chloride, beryllium chloride, magnesium chloride, Calcium chloride, strontium chloride, barium chloride, radium chloride, zinc chloride, copper chloride, nickel chloride, cobalt chloride, ferric chloride, ferrous chloride, manganese chloride, chromium chloride, chlorine Vanadium chloride, titanium tetrachloride, scandium chloride, aluminum chloride, gallium chloride, indium chloride, thallium chloride, tin chloride, lead chloride, cadmium chloride, palladium chloride, rhodium chloride, chloride At least one of ruthenium, zirconium chloride, hafnium chloride, osmium chloride, platinum chloride, gold chloride, and mercury chloride. Therefore, in the process of jet spinning, under the action of chloride, a composite fiber aerogel material with a layered structure can be obtained, thereby greatly improving the compressibility of the carbon fiber-based aerogel material.
根据本发明的实施例,为了促进无机前驱体的水解,纺丝前驱体混合液中进一步包括催化剂。在本发明的实施例中,所述催化剂选自磷酸、硫酸、盐酸、硝酸、甲酸、醋酸、氢氟酸、高氯酸、三氟乙酸、柠檬酸、草酸和马来酸中的至少一种。由此,在上述催化剂的作用下,无机前驱体可以快速、有效地、更充分地水解成无机氧化物,得到复合纤维气凝胶材料,进而有利于后续得到性能优异的碳纤维基气凝胶材料。According to an embodiment of the present invention, in order to promote the hydrolysis of the inorganic precursor, a catalyst is further included in the spinning precursor mixture. In an embodiment of the present invention, the catalyst is selected from at least one of phosphoric acid, sulfuric acid, hydrochloric acid, nitric acid, formic acid, acetic acid, hydrofluoric acid, perchloric acid, trifluoroacetic acid, citric acid, oxalic acid and maleic acid . Therefore, under the action of the above-mentioned catalyst, the inorganic precursor can be hydrolyzed into inorganic oxides quickly, effectively and more fully to obtain composite fiber aerogel materials, which is beneficial for subsequent production of carbon fiber-based aerogel materials with excellent performance. .
根据本发明的实施例,上述各个试剂、组分的混合的具体工艺没有限制要求,本领域技术人员可以根据实际需求灵活设定。在本发明的一些实施例中,将无机前驱体、催化剂和氯化物分别加入到高分子溶液中,通过搅拌得到具有一定粘度的纺丝前驱体混合液;在本发明的另一些实施例中,先将无机前驱体、催化剂和氯化物混合之后,再加入到高分子溶液中,通过搅拌得到具有一定粘度的纺丝前驱体混合液。其中,搅拌的具体方式也没有限定要求,可以是机械搅拌,也可以是磁力搅拌,在此不作限制要求。According to the embodiments of the present invention, there is no restriction on the specific process of mixing the above-mentioned reagents and components, and those skilled in the art can flexibly set according to actual needs. In some embodiments of the present invention, the inorganic precursor, catalyst and chloride are added to the polymer solution separately, and a spinning precursor mixture with a certain viscosity is obtained by stirring; in other embodiments of the present invention, The inorganic precursor, catalyst and chloride are mixed first, and then added to the polymer solution, and a spinning precursor mixture with a certain viscosity is obtained by stirring. Among them, the specific method of stirring is also not limited. It can be mechanical stirring or magnetic stirring, which is not limited here.
根据本发明的实施例,为了得到性能较佳的碳纤维基气凝胶材料,纺丝前驱体混合液包括:2~30重量份的高分子材料;100重量份的溶剂;0.5~100重量份的无机前驱体;0.001~1重量份的催化剂;及1~100重量份的氯化物。由此,上述配比制备的碳纤维基气凝胶材料具有良好的可压缩性、柔韧性,具有各向异性的层状结构,其中,氯化物的用量可以有效保证碳纤维基气凝胶的层状结构。若氯化物的用量偏低,则碳纤维基气凝胶材料的层状结构不明显,导致其可压缩性能相对较差;若氯化物的用量偏多,也会造成气凝胶材料的可压缩性能变差。According to an embodiment of the present invention, in order to obtain a carbon fiber-based aerogel material with better performance, the spinning precursor mixture includes: 2-30 parts by weight of polymer material; 100 parts by weight of solvent; 0.5-100 parts by weight Inorganic precursor; 0.001 to 1 parts by weight of catalyst; and 1 to 100 parts by weight of chloride. Therefore, the carbon fiber-based aerogel material prepared by the above ratio has good compressibility, flexibility, and an anisotropic layered structure, wherein the amount of chloride can effectively ensure the layered shape of the carbon fiber-based aerogel structure. If the amount of chloride is too low, the layered structure of the carbon fiber-based aerogel material is not obvious, resulting in relatively poor compressibility; if the amount of chloride is too high, it will also cause the compressibility of the aerogel material Getting worse.
S200:对纺丝前驱体混合液进行喷射纺丝,得到复合纤维气凝胶。在该过程中,在氯化物的作用下,得到的复合纤维气凝胶为多层堆叠的层状结构,使其具有各向异性,使得最终得到的碳纤维基气凝胶材料可以裁剪成所需的形状,堆叠得到所需的厚度。其中,“各向异性”是指相对碳纤维基气凝胶材料中碳纤维层,从不同方向压缩碳纤维基气凝胶材料,其可压缩性不同,恢复性能不同,比如从垂直于碳纤维层的方向压缩碳纤维基气凝胶材料,碳纤维基气凝胶材料可以完全恢复原状,而从平行于碳纤维层的方向压缩碳纤维基气凝胶材料,碳纤维基气凝胶材料则不能恢复原状。S200: Jet spinning the spinning precursor mixture to obtain composite fiber aerogel. In this process, under the action of chloride, the obtained composite fiber aerogel has a multi-layer stacked layered structure, which makes it anisotropic, so that the final carbon fiber-based aerogel material can be cut to the desired The shape is stacked to get the desired thickness. Among them, "anisotropy" means that the carbon fiber-based aerogel material is compressed from different directions relative to the carbon fiber layer in the carbon fiber-based aerogel material, and its compressibility is different, and the recovery performance is different, such as compression from a direction perpendicular to the carbon fiber layer Carbon fiber-based aerogel materials, carbon fiber-based aerogel materials can be completely restored to their original state, while compressing carbon fiber-based aerogel materials from a direction parallel to the carbon fiber layer, carbon fiber-based aerogel materials cannot be restored to their original state.
根据本发明的实施例,利用喷射纺丝技术对纺丝前驱体混合液进行纺丝,利用压缩空气将所述纺丝前驱体混合液从喷射纺丝设备的喷丝口喷出,具体的:喷射纺丝采用一对同轴喷嘴,利用压缩空气将纺丝前驱体混合液经内喷嘴挤出,高速气流经外喷嘴喷出,纺丝前驱体混合液在高速气流的剪切作用下形成聚合物射流,在到达接收装置的过程中,射流进一步发生分裂、牵伸、细化,同时溶剂不断挥发,纤维成形固化并收集于接收装置(也可称“接收器”)上。与静电纺丝相比,喷射纺丝设备简单,以高速气流作为驱动力,不需要高压静电场,具有更高的纺丝效率,并且复合纤维气凝胶可以沉积在任何基底上。因此,采用喷射纺丝技术大规模制备具有良好柔韧性和导电性的碳纤维基气凝胶材料具有重要意义。According to the embodiment of the present invention, the spinning precursor mixture is spun using the jet spinning technology, and the spinning precursor mixture is ejected from the spinneret of the jet spinning equipment by compressed air, specifically: Jet spinning adopts a pair of coaxial nozzles, using compressed air to extrude the spinning precursor mixture through the inner nozzle, and the high-speed airflow is ejected through the outer nozzle. The spinning precursor mixture is polymerized under the shearing action of the high-speed airflow. When the material jet reaches the receiving device, the jet further splits, stretches, and refines. At the same time, the solvent continuously volatilizes, and the fibers are formed and solidified and collected on the receiving device (also called "receiver"). Compared with electrospinning, the jet spinning equipment is simple, uses high-speed airflow as the driving force, does not require high-voltage electrostatic field, has higher spinning efficiency, and the composite fiber aerogel can be deposited on any substrate. Therefore, it is of great significance to use jet spinning technology to prepare large-scale carbon fiber-based aerogel materials with good flexibility and conductivity.
根据本发明的实施例,接收装置的具体种类没有限制要求,本领域技术人员可以根据实际需求灵活选择。在本发明的一些实施例中,接收装置包括但不限于金属网、塑料网和无纺布。According to the embodiment of the present invention, there is no restriction on the specific type of the receiving device, and those skilled in the art can flexibly choose according to actual needs. In some embodiments of the present invention, the receiving device includes but is not limited to metal mesh, plastic mesh, and non-woven fabric.
根据本发明的实施例,为了得到柔韧性佳、导电性好等性能优异的碳纤维基气凝胶材料,在喷射纺丝中,纺丝前驱体混合液的挤出速度为0.1~15毫升/小时(比如0.1mL/h、0.5mL/h、1mL/h、2mL/h、3mL/h、4mL/h、5mL/h、6mL/h、7mL/h、8mL/h、9mL/h、10mL/h、11mL/h、12mL/h、13mL/h、14mL/h、15mL/h),喷丝口与接收器之间的距离为20~100厘米(比如20cm、30cm、40cm、50cm、60cm、70cm、80cm、90cm、100cm),压缩空气的气流流速为1~50米/秒(比如1m/s、5m/s、10m/s、15m/s、20m/s、25m/s、30m/s、35m/s、40m/s、45m/s、50m/s)。由此,可以制备性能优异的碳纤维基气凝胶材料。According to the embodiment of the present invention, in order to obtain a carbon fiber-based aerogel material with excellent flexibility and conductivity, in jet spinning, the extrusion speed of the spinning precursor mixture is 0.1-15 ml/h (E.g. 0.1mL/h, 0.5mL/h, 1mL/h, 2mL/h, 3mL/h, 4mL/h, 5mL/h, 6mL/h, 7mL/h, 8mL/h, 9mL/h, 10mL/ h, 11mL/h, 12mL/h, 13mL/h, 14mL/h, 15mL/h), the distance between the spinneret and the receiver is 20-100 cm (such as 20cm, 30cm, 40cm, 50cm, 60cm, 70cm, 80cm, 90cm, 100cm), the compressed air flow velocity is 1-50m/s (such as 1m/s, 5m/s, 10m/s, 15m/s, 20m/s, 25m/s, 30m/s , 35m/s, 40m/s, 45m/s, 50m/s). Thus, a carbon fiber-based aerogel material with excellent performance can be prepared.
S300:对复合纤维气凝胶依次进行预氧化处理和碳化处理,得到各向异性层状碳纤维基气凝胶材料。在该过程中,通过预氧化处理和碳化处理,高分子材料裂解,脱去氢和氧等元素,形成碳纤维,得到碳纤维基气凝胶材料,使得层状结构的碳纤维基气凝胶材料具有优异的导电性。S300: Perform pre-oxidation treatment and carbonization treatment on the composite fiber aerogel in sequence to obtain an anisotropic layered carbon fiber-based aerogel material. In this process, through the pre-oxidation treatment and carbonization treatment, the polymer material is pyrolyzed, and the elements such as hydrogen and oxygen are removed to form carbon fibers. The carbon fiber-based aerogel material is obtained, making the layered structure of the carbon fiber-based aerogel material excellent The conductivity.
根据本发明的实施例,为了充分地将高分子材料裂解形成碳纤维,预氧化处理和碳化处理的条件分别为:在空气中以0.5~10℃/min(比如0.5℃/min、1℃/min、2℃/min、3℃/min、4℃/min、5℃/min、6℃/min、7℃/min、8℃/min、9℃/min、10℃/min)的升温速度升至180℃~300℃(比如180℃、200℃、230℃、250℃、280℃或300℃),进行预氧化处理0.5~3小时(比如0.5小时、1小时、1.5小时、2小时、2.5小时或3小时);在惰性气体氛围中,以0.5~10℃/min(比如0.5℃/min、1℃/min、2℃/min、3℃/min、4℃/min、5℃/min、6℃/min、7℃/min、8℃/min、9℃/min、10℃/min)的升温速度升至700℃~1500℃(比如700℃、800℃、 900℃、1000℃、1100℃、1200℃、1300℃、1400℃或1500℃),进行碳化处理0.5~3小时(比如0.5小时、1小时、1.5小时、2小时、2.5小时或3小时),之后降温至室温,其中的具体参数本领域技术人员可以根据实际情况灵活设定即可。需要说明的是,碳化处理的温度可以是在预氧化温度的基础上进行升温,由此,可以缩短工艺时长,节省能源。According to the embodiment of the present invention, in order to fully pyrolyze the polymer material to form carbon fiber, the conditions of the pre-oxidation treatment and the carbonization treatment are respectively: 0.5-10℃/min (such as 0.5℃/min, 1℃/min) in the air , 2℃/min, 3℃/min, 4℃/min, 5℃/min, 6℃/min, 7℃/min, 8℃/min, 9℃/min, 10℃/min) To 180℃~300℃ (such as 180℃, 200℃, 230℃, 250℃, 280℃ or 300℃), carry out pre-oxidation treatment for 0.5~3 hours (such as 0.5 hour, 1 hour, 1.5 hours, 2 hours, 2.5 Hours or 3 hours); In an inert gas atmosphere, 0.5~10℃/min (such as 0.5℃/min, 1℃/min, 2℃/min, 3℃/min, 4℃/min, 5℃/min , 6°C/min, 7°C/min, 8°C/min, 9°C/min, 10°C/min) rise to 700°C~1500°C (such as 700°C, 800°C, 900°C, 1000°C, 1100 ℃, 1200 ℃, 1300 ℃, 1400 ℃ or 1500 ℃), carry out carbonization treatment for 0.5 to 3 hours (such as 0.5 hour, 1 hour, 1.5 hours, 2 hours, 2.5 hours or 3 hours), then cool to room temperature, where Those skilled in the art can flexibly set the specific parameters according to the actual situation. It should be noted that the temperature of the carbonization treatment can be raised on the basis of the pre-oxidation temperature, thereby shortening the process time and saving energy.
根据本发明的实施例,上述碳纤维基气凝胶材料的制备方法简单,易操作,制备成本低、效率高,易于工业化生产;由上述方法制备的碳纤维基气凝胶材料是由多层堆叠的微纤维构成,具有各向异性的层状结构,可以裁切成所需的任意形状,以及堆叠成所需的厚度;而且制备的碳纤维基气凝胶材料具有良好的柔韧性和可压缩性;碳纤维基气凝胶材料的层状结构和碳组分使得气凝胶材料具有良好的导电性,并且电导率随压缩应变的增加而增大,进而使其在应力传感、电磁屏蔽、空气过滤、能源存储等领域有着广阔的应用前景。According to the embodiment of the present invention, the preparation method of the above-mentioned carbon fiber-based aerogel material is simple, easy to operate, low-cost, high-efficiency, and easy for industrial production; the carbon-fiber-based aerogel material prepared by the above method is stacked by multiple layers It is composed of microfibers and has an anisotropic layered structure, which can be cut into any desired shape and stacked to a desired thickness; and the prepared carbon fiber-based aerogel material has good flexibility and compressibility; The layered structure and carbon component of carbon fiber-based aerogel materials make the aerogel materials have good electrical conductivity, and the electrical conductivity increases with the increase of compressive strain, which in turn makes it useful for stress sensing, electromagnetic shielding, and air filtration. , Energy storage and other fields have broad application prospects.
在本发明的又一方面,本发明提供了一种各向异性层状碳纤维基气凝胶材料。根据本发明的实施例,所述各向异性层状碳纤维基气凝胶材料是由前面所述的方法制备得到的。由此,该碳纤维基气凝胶材料是由多层堆叠的微纤维构成,具有各向异性的层状结构,可以裁切成所需的任意形状,以及堆叠成所需的厚度;而且,该碳纤维基气凝胶材料具有良好的柔韧性和可压缩性;碳纤维基气凝胶材料的层状结构和碳组分使得气凝胶材料具有良好的导电性,并且电导率随压缩应变的增加而增大,进而使其在应力传感、电磁屏蔽、空气过滤、能源存储等领域有着广阔的应用前景。In another aspect of the present invention, the present invention provides an anisotropic layered carbon fiber-based aerogel material. According to an embodiment of the present invention, the anisotropic layered carbon fiber-based aerogel material is prepared by the aforementioned method. Thus, the carbon fiber-based aerogel material is composed of multiple stacked microfibers and has an anisotropic layered structure, which can be cut into any desired shape and stacked to a desired thickness; moreover, the Carbon fiber-based aerogel materials have good flexibility and compressibility; the layered structure and carbon component of carbon fiber-based aerogel materials make the aerogel materials have good electrical conductivity, and the electrical conductivity increases with the increase in compression strain. Increase, and make it have broad application prospects in stress sensing, electromagnetic shielding, air filtration, energy storage and other fields.
根据本发明的实施例,碳纤维基气凝胶材料的体积密度为5~200mg/cm 3(比如5mg/cm 3、25mg/cm 3、50mg/cm 3、75mg/cm 3、100mg/cm 3、125mg/cm 3、150mg/cm 3、175mg/cm 3、200mg/cm 3、),碳纤维基气凝胶材料中纤维的平均直径为0.2~10微米(比如0.2微米、0.5微米、1微米、2微米、4微米、6微米、8微米或10微米)。由此,碳纤维基气凝胶材料的体积密度和纤维直径的范围较宽,本领域技术人员可以根据不同的需求和应用,制备体积密度和纤维直径不同的碳纤维基气凝胶材料,满足不同的市场需求。 According to an embodiment of the present invention, the bulk density of the carbon fiber-based aerogel material is 5 to 200 mg/cm 3 (such as 5 mg/cm 3 , 25 mg/cm 3 , 50 mg/cm 3 , 75 mg/cm 3 , 100 mg/cm 3 , 125mg/cm 3 , 150mg/cm 3 , 175mg/cm 3 , 200mg/cm 3 , ), the average diameter of the fibers in the carbon fiber-based aerogel material is 0.2-10 microns (such as 0.2 microns, 0.5 microns, 1 microns, 2 Microns, 4 microns, 6 microns, 8 microns or 10 microns). As a result, the bulk density and fiber diameter of carbon fiber-based aerogel materials have a wide range. Those skilled in the art can prepare carbon fiber-based aerogel materials with different bulk densities and fiber diameters according to different needs and applications to meet different requirements. Market demand.
实施例Example
实施例1Example 1
一种各向异性层状碳纤维基气凝胶材料的制备方法,采用以下工艺步骤:A preparation method of anisotropic layered carbon fiber-based aerogel material adopts the following process steps:
(1)高分子溶液配制:将15g聚乙烯醇缩丁醛添加到100g去离子水中,在90℃条件下以800rpm的转速搅拌溶解1h,得到高分子材料与溶剂质量比为15:100的聚乙烯醇缩丁醛溶液;(1) Preparation of polymer solution: 15g of polyvinyl butyral was added to 100g of deionized water, stirred and dissolved at 800rpm at 90℃ for 1h to obtain a polymer with a polymer material and solvent mass ratio of 15:100. Vinyl butyral solution;
(2)纺丝前驱体混合液配制:将35g氧氯化锆、0.2g硝酸、40g氯化铁添加到上述聚乙烯醇缩丁醛溶液中,通过搅拌得到具有一定粘度的纺丝前驱体混合液;(2) Preparation of spinning precursor mixture: 35g of zirconium oxychloride, 0.2g of nitric acid, and 40g of ferric chloride were added to the above polyvinyl butyral solution, and a spinning precursor with a certain viscosity was obtained by stirring. liquid;
(3)喷射纺丝:采用喷射纺丝技术用流速为5m/s的压缩空气将纺丝前驱体混合液以5mL/h的速度从喷丝口喷出,得到的纤维沉积在距离喷丝口60cm的金属网接收器上,得到复合纤维气凝胶;(3) Jet spinning: using jet spinning technology to use compressed air with a flow rate of 5m/s to eject the spinning precursor mixture from the spinneret at a speed of 5mL/h, and the resulting fiber is deposited at a distance from the spinneret Obtain composite fiber aerogel on a 60cm metal mesh receiver;
(4)预氧化和碳化:将得到的复合纤维气凝胶在空气气氛下以2℃/min升温至300℃进行预氧化处理2h,然后在氮气气氛中以5℃/min升温至800℃进行碳化处理1h,降至室温后得到各向异性层状碳纤维基气凝胶材料。(4) Pre-oxidation and carbonization: The obtained composite fiber aerogel is heated at 2°C/min to 300°C for 2h in an air atmosphere, and then heated at 5°C/min to 800°C in a nitrogen atmosphere. After carbonization treatment for 1 h, and after cooling to room temperature, an anisotropic layered carbon fiber-based aerogel material was obtained.
得到的各向异性层状碳纤维基气凝胶材料的体积密度为20mg/cm 3,纤维的平均直径为3.3μm,其扫描电镜图参照图2。 The obtained anisotropic layered carbon fiber-based aerogel material has a bulk density of 20 mg/cm 3 and an average fiber diameter of 3.3 μm. Refer to FIG. 2 for the scanning electron microscope image.
实施例2Example 2
一种各向异性层状碳纤维基气凝胶材料的制备方法,采用以下工艺步骤:A preparation method of anisotropic layered carbon fiber-based aerogel material adopts the following process steps:
(1)高分子溶液配制:将5g聚氧化乙烯添加到100g去离子水中,在90℃条件下以800rpm的转速搅拌溶解1h,得到高分子材料与溶剂质量比为5:100的聚氧化乙烯溶液;(1) Preparation of polymer solution: Add 5g of polyethylene oxide to 100g of deionized water, stir and dissolve at 800 rpm at 90°C for 1 hour to obtain a polyethylene oxide solution with a polymer material to solvent mass ratio of 5:100 ;
(2)纺丝前驱体混合液配制:将50g乙酸锆、0.1g磷酸、40g氯化镁添加到上述聚氧化乙烯溶液中,通过搅拌得到具有一定粘度的纺丝前驱体混合液;(2) Preparation of spinning precursor mixture: adding 50 g of zirconium acetate, 0.1 g of phosphoric acid, and 40 g of magnesium chloride to the above polyethylene oxide solution, and stirring to obtain a spinning precursor mixture with a certain viscosity;
(3)喷射纺丝:采用喷射纺丝技术用流速为5m/s的压缩空气将纺丝前驱体混合液以5mL/h的速度从喷丝口喷出,得到的纤维沉积在距离喷丝口60cm的金属网接收器上,得到复合纤维气凝胶;(3) Jet spinning: using jet spinning technology to use compressed air with a flow rate of 5m/s to eject the spinning precursor mixture from the spinneret at a speed of 5mL/h, and the resulting fiber is deposited at a distance from the spinneret Obtain composite fiber aerogel on a 60cm metal mesh receiver;
(4)预氧化和碳化:将得到的复合纤维气凝胶在空气气氛下以1℃/min升温至300℃进行预氧化处理2h,然后在氮气气氛中以5℃/min升温至850℃进行碳化处理1h,降至室温后得到各向异性层状碳纤维基气凝胶材料。(4) Pre-oxidation and carbonization: The obtained composite fiber aerogel is heated at 1℃/min to 300℃ for 2h in air atmosphere, and then heated at 5℃/min to 850℃ in nitrogen atmosphere. After carbonization treatment for 1 h, and after cooling to room temperature, an anisotropic layered carbon fiber-based aerogel material was obtained.
所得产品各向异性层状碳纤维基气凝胶材料的体积密度为19mg/cm 3,纤维的平均直径为3.6μm。 The resulting product has an anisotropic layered carbon fiber-based aerogel material with a bulk density of 19 mg/cm 3 and an average fiber diameter of 3.6 μm.
实施例3Example 3
一种各向异性层状碳纤维基气凝胶材料的制备方法,采用以下工艺步骤:A preparation method of anisotropic layered carbon fiber-based aerogel material adopts the following process steps:
(1)高分子溶液配制:将10g聚乙烯醇添加到100g去离子水中,在90℃条件下以800rpm的转速搅拌溶解1h,得到高分子材料与溶剂质量比为10:100的聚乙烯醇溶液;(1) Preparation of polymer solution: Add 10g of polyvinyl alcohol to 100g of deionized water, stir and dissolve at 800rpm at 90°C for 1h to obtain a polyvinyl alcohol solution with a polymer material to solvent mass ratio of 10:100 ;
(2)纺丝前驱体混合液配制:将40g正硅酸乙酯、0.2g磷酸、40g氯化铝添加到上述聚乙烯醇溶液中,通过搅拌得到具有一定粘度的纺丝前驱体混合液;(2) Preparation of the spinning precursor mixture: adding 40 g of ethyl orthosilicate, 0.2 g of phosphoric acid, and 40 g of aluminum chloride to the above polyvinyl alcohol solution, and stirring to obtain a spinning precursor mixture with a certain viscosity;
(3)喷射纺丝:采用喷射纺丝技术用流速为5m/s的压缩空气将纺丝前驱体混合液以5mL/h的速度从喷丝口喷出,得到的纤维沉积在距离喷丝口60cm的金属网接收器上,得到复合纤维气凝胶;(3) Jet spinning: using jet spinning technology to use compressed air with a flow rate of 5m/s to eject the spinning precursor mixture from the spinneret at a speed of 5mL/h, and the resulting fiber is deposited at a distance from the spinneret Obtain composite fiber aerogel on a 60cm metal mesh receiver;
(4)预氧化和碳化:将得到的复合纤维气凝胶在空气气氛下以1.5℃/min升温至300℃进行预氧化处理1h,然后在氮气气氛中以5℃/min升温至900℃进行碳化处理2h,降至室温后得到各向异性层状碳纤维基气凝胶材料。(4) Pre-oxidation and carbonization: The obtained composite fiber aerogel is heated at 1.5°C/min to 300°C for 1h in an air atmosphere, and then heated at 5°C/min to 900°C in a nitrogen atmosphere. The carbonization treatment was carried out for 2 hours, and the anisotropic layered carbon fiber-based aerogel material was obtained after being cooled to room temperature.
所得产品各向异性层状碳纤维基气凝胶材料的体积密度为17mg/cm 3,纤维的平均直径为3.9μm。 The resulting product has an anisotropic layered carbon fiber-based aerogel material with a bulk density of 17 mg/cm 3 and an average fiber diameter of 3.9 μm.
实施例4Example 4
一种各向异性层状碳纤维基气凝胶材料的制备方法,采用以下工艺步骤:A preparation method of anisotropic layered carbon fiber-based aerogel material adopts the following process steps:
(1)高分子溶液配制:将5g羧甲基纤维素添加到100g去离子水中,在60℃条件下以800rpm的转速搅拌溶解1h,得到高分子材料与溶剂质量比为5:100的羧甲基纤维素溶液;(1) Preparation of polymer solution: add 5 g of carboxymethyl cellulose to 100 g of deionized water, stir and dissolve at 800 rpm at 60°C for 1 hour to obtain a polymer material and solvent mass ratio of 5:100 carboxymethyl Base cellulose solution;
(2)纺丝前驱体混合液配制:将40g乙酸锆、0.2g盐酸、35g氯化镁添加到上述羧甲基纤维素溶液中,通过搅拌得到具有一定粘度的纺丝前驱体混合液;(2) Preparation of spinning precursor mixture: 40g of zirconium acetate, 0.2g of hydrochloric acid, and 35g of magnesium chloride are added to the above carboxymethyl cellulose solution, and a spinning precursor mixture with a certain viscosity is obtained by stirring;
(3)喷射纺丝:采用喷射纺丝技术用流速为5m/s的压缩空气将纺丝前驱体混合液以5mL/h的速度从喷丝口喷出,得到的纤维沉积在距离喷丝口60cm的金属网接收器上,得到复合纤维气凝胶;(3) Jet spinning: using jet spinning technology to use compressed air with a flow rate of 5m/s to eject the spinning precursor mixture from the spinneret at a speed of 5mL/h, and the resulting fiber is deposited at a distance from the spinneret Obtain composite fiber aerogel on a 60cm metal mesh receiver;
(4)预氧化和碳化:将得到的复合纤维气凝胶在空气气氛下以1℃/min升温至280℃进行预氧化处理1h,然后在氮气气氛中以5℃/min升温至850℃进行碳化处理1h,降至室温后得到各向异性层状碳纤维基气凝胶材料。(4) Pre-oxidation and carbonization: The obtained composite fiber aerogel is heated at 1°C/min to 280°C for 1h in an air atmosphere, and then heated at 5°C/min to 850°C in a nitrogen atmosphere. After carbonization treatment for 1 h, and after cooling to room temperature, an anisotropic layered carbon fiber-based aerogel material was obtained.
所得产品各向异性层状碳纤维基气凝胶材料的体积密度为22mg/cm 3,纤维的平均直径为3.6μm。 The resulting product has an anisotropic layered carbon fiber-based aerogel material with a bulk density of 22 mg/cm 3 and an average fiber diameter of 3.6 μm.
实施例5Example 5
一种各向异性层状碳纤维基气凝胶材料的制备方法,采用以下工艺步骤:A preparation method of anisotropic layered carbon fiber-based aerogel material adopts the following process steps:
(1)高分子溶液配制:将15g聚乙烯吡咯烷酮添加到100g去离子水中,在60℃条件下以800rpm的转速搅拌溶解1h,得到高分子材料与溶剂质量比为15:100的聚乙烯吡咯烷酮溶液;(1) Preparation of polymer solution: Add 15g of polyvinylpyrrolidone to 100g of deionized water, stir and dissolve at 800rpm at 60℃ for 1h to obtain a solution of polyvinylpyrrolidone with a mass ratio of polymer material to solvent of 15:100 ;
(2)纺丝前驱体混合液配制:将40g氧氯化锆、0.1g磷酸、40g氯化镁添加到上述聚乙烯吡咯烷酮溶液中,通过搅拌得到具有一定粘度的纺丝前驱体混合液;(2) Preparation of spinning precursor mixture: 40g of zirconium oxychloride, 0.1g of phosphoric acid, and 40g of magnesium chloride are added to the above polyvinylpyrrolidone solution, and a spinning precursor mixture with a certain viscosity is obtained by stirring;
(3)喷射纺丝:采用溶液喷射纺丝技术用流速为5m/s的压缩空气将纺丝前驱体混合液以5mL/h的速度从喷丝口喷出,得到的纤维沉积在距离喷丝口60cm的金属网接收器上,得到复合纤维气凝胶;(3) Jet spinning: using solution jet spinning technology to use compressed air with a flow rate of 5m/s to eject the spinning precursor mixture from the spinneret at a speed of 5mL/h, and the resulting fibers are deposited in the distance spinning The composite fiber aerogel is obtained on the metal mesh receiver with an opening of 60 cm;
(4)预氧化和碳化:将得到的复合纤维气凝胶在空气气氛下以1℃/min升温至300℃进行预氧化处理2h,然后在氮气气氛中以5℃/min升温至900℃进行碳化处理2h,降至室温后得到各向异性层状碳纤维基气凝胶材料。(4) Pre-oxidation and carbonization: The obtained composite fiber aerogel is heated at 1°C/min to 300°C for 2h in an air atmosphere, and then heated at 5°C/min to 900°C in a nitrogen atmosphere. The carbonization treatment was carried out for 2 hours, and the anisotropic layered carbon fiber-based aerogel material was obtained after being cooled to room temperature.
所得产品各向异性层状碳纤维基气凝胶材料的体积密度为21mg/cm 3,纤维的平均直径为4.3μm。 The resulting product has an anisotropic layered carbon fiber-based aerogel material with a bulk density of 21 mg/cm 3 and an average fiber diameter of 4.3 μm.
在本说明书的描述中,参考术语“一个实施例”、“一些实施例”、“示例”、“具体示例”或“一些示例”等的描述意指结合该实施例或示例描述的具体特征、结构、材料或者特点包含于本发明的至少一个实施例或示例中。在本说明书中,对上述术语的示意性表述不必须针对的是相同的实施例或示例。而且,描述的具体特征、结构、材料或者特点可以在任一个或多个实施例或示例中以合适的方式结合。此外,在不相互矛盾的情况下,本领域的技术人员可以将本说明书中描述的不同实施例或示例以及不同实施例或示例的特征进行结合和组合。In the description of this specification, descriptions with reference to the terms "one embodiment", "some embodiments", "examples", "specific examples" or "some examples" etc. mean the specific features described in conjunction with the embodiment or example, The structure, material or feature is included in at least one embodiment or example of the present invention. In this specification, the schematic representations of the above terms do not necessarily refer to the same embodiment or example. Moreover, the described specific features, structures, materials or characteristics can be combined in any one or more embodiments or examples in a suitable manner. In addition, those skilled in the art can combine and combine the different embodiments or examples and the characteristics of the different embodiments or examples described in this specification without contradicting each other.
尽管上面已经示出和描述了本发明的实施例,可以理解的是,上述实施例是示例性的,不能理解为对本发明的限制,本领域的普通技术人员在本发明的范围内可以对上述实施例进行变化、修改、替换和变型。Although the embodiments of the present invention have been shown and described above, it can be understood that the above-mentioned embodiments are exemplary and should not be construed as limiting the present invention. Those of ordinary skill in the art can comment on the foregoing within the scope of the present invention. The embodiment undergoes changes, modifications, substitutions and modifications.

Claims (10)

  1. 一种各向异性层状碳纤维基气凝胶材料的制备方法,其特征在于,包括:A method for preparing an anisotropic layered carbon fiber-based aerogel material, which is characterized in that it comprises:
    将高分子溶液、无机前驱体和氯化物混合,得到纺丝前驱体混合液;Mixing the polymer solution, the inorganic precursor and the chloride to obtain a spinning precursor mixture;
    对所述纺丝前驱体混合液进行喷射纺丝,得到复合纤维气凝胶;Jet spinning the spinning precursor mixture to obtain a composite fiber aerogel;
    对所述复合纤维气凝胶依次进行预氧化处理和碳化处理,得到各向异性层状碳纤维基气凝胶材料。The composite fiber aerogel is sequentially subjected to pre-oxidation treatment and carbonization treatment to obtain an anisotropic layered carbon fiber-based aerogel material.
  2. 根据权利要求1所述的方法,其特征在于,所述高分子溶液包括高分子材料和溶剂,其中,所述高分子材料与所述溶剂的质量比为(2~30):100。The method according to claim 1, wherein the polymer solution comprises a polymer material and a solvent, wherein the mass ratio of the polymer material to the solvent is (2-30):100.
  3. 根据权利要求1或2所述的方法,其特征在于,所述纺丝前驱体混合液中进一步包括催化剂。The method of claim 1 or 2, wherein the spinning precursor mixture further includes a catalyst.
  4. 根据权利要求3所述的方法,其特征在于,所述纺丝前驱体混合液包括:The method of claim 3, wherein the spinning precursor mixture comprises:
    2~30重量份的所述高分子材料;2-30 parts by weight of the polymer material;
    100重量份的所述溶剂;100 parts by weight of the solvent;
    0.5~100重量份的所述无机前驱体;0.5-100 parts by weight of the inorganic precursor;
    0.001~1重量份的所述催化剂;及0.001 to 1 part by weight of the catalyst; and
    1~100重量份的所述氯化物。1-100 parts by weight of the chloride.
  5. 根据权利要求4所述的方法,其特征在于,所述高分子材料选自聚乙烯醇、聚乙二醇、聚氨酯、聚丙烯酸、聚乙烯吡咯烷酮、醋酸纤维素、甲基纤维素、羧甲基纤维素、聚偏氟乙烯、聚甲基丙烯酸甲酯、聚丙烯酰胺、聚氧化乙烯、聚乳酸、聚酰胺、聚己内酯、聚乙烯醇缩丁醛、聚苯胺、聚酰亚胺和聚碳酸酯中的至少一种;The method according to claim 4, wherein the polymer material is selected from polyvinyl alcohol, polyethylene glycol, polyurethane, polyacrylic acid, polyvinylpyrrolidone, cellulose acetate, methyl cellulose, carboxymethyl Cellulose, polyvinylidene fluoride, polymethyl methacrylate, polyacrylamide, polyethylene oxide, polylactic acid, polyamide, polycaprolactone, polyvinyl butyral, polyaniline, polyimide and poly At least one of carbonates;
    任选地,所述溶剂选自水、甲酸、四氢呋喃、丙酮、丁酮、正己烷、环己烷、正庚烷、乙腈、N-甲基吡咯烷酮、1,2-丙二醇、氯仿、二氯甲烷、1,2-二氯乙烷、甲醇、乙醇、异丙醇、叔丁醇、正丁醇、甲苯、二甲苯、乙二胺、二甲基亚砜、N,N-二甲基甲酰胺、N,N-二甲基乙酰胺和四氯化碳中的至少一种;Optionally, the solvent is selected from water, formic acid, tetrahydrofuran, acetone, butanone, n-hexane, cyclohexane, n-heptane, acetonitrile, N-methylpyrrolidone, 1,2-propanediol, chloroform, dichloromethane , 1,2-Dichloroethane, methanol, ethanol, isopropanol, tert-butanol, n-butanol, toluene, xylene, ethylenediamine, dimethyl sulfoxide, N,N-dimethylformamide , At least one of N,N-dimethylacetamide and carbon tetrachloride;
    任选地,所述无机前驱体为氧氯化锆、乙酸锆、异丙醇铝、正丙醇锆、正硅酸乙酯和正硅酸甲酯中的至少一种;Optionally, the inorganic precursor is at least one of zirconium oxychloride, zirconium acetate, aluminum isopropoxide, zirconium n-propoxide, ethyl orthosilicate, and methyl orthosilicate;
    任选地,所述催化剂选自磷酸、硫酸、盐酸、硝酸、甲酸、醋酸、氢氟酸、高氯酸、三氟乙酸、柠檬酸、草酸和马来酸中的至少一种。Optionally, the catalyst is selected from at least one of phosphoric acid, sulfuric acid, hydrochloric acid, nitric acid, formic acid, acetic acid, hydrofluoric acid, perchloric acid, trifluoroacetic acid, citric acid, oxalic acid and maleic acid.
  6. 根据权利要求1~5中任一项所述的方法,其特征在于,所述氯化物选自氯化锂、氯 化钠、氯化钾、氯化铷、氯化铯、氯化铍、氯化镁、氯化钙、氯化锶、氯化钡、氯化镭、氯化锌、氯化铜、氯化镍、氯化钴、氯化铁、氯化亚铁、氯化锰、氯化铬、氯化钒、四氯化钛、氯化钪、氯化铝、氯化镓、氯化铟、氯化铊、氯化锡、氯化铅、氯化镉、氯化钯、氯化铑、氯化钌、氯化锆、氯化铪、三氯化锇、氯化铂、氯化金和氯化汞中的至少一种。The method according to any one of claims 1 to 5, wherein the chloride is selected from lithium chloride, sodium chloride, potassium chloride, rubidium chloride, cesium chloride, beryllium chloride, magnesium chloride , Calcium chloride, strontium chloride, barium chloride, radium chloride, zinc chloride, copper chloride, nickel chloride, cobalt chloride, ferric chloride, ferrous chloride, manganese chloride, chromium chloride, Vanadium chloride, titanium tetrachloride, scandium chloride, aluminum chloride, gallium chloride, indium chloride, thallium chloride, tin chloride, lead chloride, cadmium chloride, palladium chloride, rhodium chloride, chlorine At least one of ruthenium chloride, zirconium chloride, hafnium chloride, osmium chloride, platinum chloride, gold chloride, and mercury chloride.
  7. 根据权利要求1~6中任一项所述的方法,其特征在于,利用压缩空气将所述纺丝前驱体混合液从喷射纺丝设备的喷丝口喷出,在所述喷射纺丝中,所述纺丝前驱体混合液的挤出速度为0.1~15毫升/小时,所述喷丝口与接收器之间的距离为20~100厘米,所述压缩空气的气流流速为1~50米/秒。The method according to any one of claims 1 to 6, characterized in that compressed air is used to eject the spinning precursor mixture from the spinneret of a jet spinning device, and in the jet spinning , The extrusion speed of the spinning precursor mixture is 0.1-15 ml/h, the distance between the spinneret and the receiver is 20-100 cm, and the air flow rate of the compressed air is 1-50 Meters per second.
  8. 根据权利要求1~7中任一项所述的方法,其特征在于,所述预氧化处理和所述碳化处理的条件分别为:在空气中以0.5~10℃/min的升温速度升至180℃~300℃,进行所述预氧化处理0.5~3小时;在惰性气体氛围中,以0.5~10℃/min的升温速度升至700℃~1500℃,进行所述碳化处理0.5~3小时,之后降温至室温。The method according to any one of claims 1 to 7, characterized in that the conditions of the pre-oxidation treatment and the carbonization treatment are respectively: in the air at a temperature rise rate of 0.5-10 °C/min to 180 ℃~300℃, carry out the pre-oxidation treatment for 0.5~3 hours; in an inert gas atmosphere, increase to 700℃~1500℃ at a heating rate of 0.5~10℃/min, carry out the carbonization treatment for 0.5~3 hours, Then cool to room temperature.
  9. 一种各向异性层状碳纤维基气凝胶材料,其特征在于,是由权利要求1~8中任一项所述的方法制备得到的。An anisotropic layered carbon fiber-based aerogel material, characterized in that it is prepared by the method according to any one of claims 1 to 8.
  10. 根据权利要求9所述的碳纤维基气凝胶材料,其特征在于,所述碳纤维基气凝胶材料的体积密度为5~200mg/cm 3The carbon fiber-based aerogel material according to claim 9, wherein the bulk density of the carbon fiber-based aerogel material is 5 to 200 mg/cm 3 ,
    任选地,所述碳纤维基气凝胶材料中纤维的平均直径为0.2~10微米。Optionally, the average diameter of the fibers in the carbon fiber-based aerogel material is 0.2-10 microns.
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