WO2013011250A1 - Graphene-based conductive composite fibres - Google Patents

Graphene-based conductive composite fibres Download PDF

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Publication number
WO2013011250A1
WO2013011250A1 PCT/FR2012/051748 FR2012051748W WO2013011250A1 WO 2013011250 A1 WO2013011250 A1 WO 2013011250A1 FR 2012051748 W FR2012051748 W FR 2012051748W WO 2013011250 A1 WO2013011250 A1 WO 2013011250A1
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Prior art keywords
graphene
fiber
coagulation
composite fibers
dispersion
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PCT/FR2012/051748
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French (fr)
Inventor
Patrice Gaillard
Alexander Korzhenko
Patrick Delprat
Serge Bordere
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Arkema France
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Publication of WO2013011250A1 publication Critical patent/WO2013011250A1/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
    • D01F1/00General methods for the manufacture of artificial filaments or the like
    • D01F1/02Addition of substances to the spinning solution or to the melt
    • D01F1/09Addition of substances to the spinning solution or to the melt for making electroconductive or anti-static filaments
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B82NANOTECHNOLOGY
    • B82YSPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
    • B82Y30/00Nanotechnology for materials or surface science, e.g. nanocomposites
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B82NANOTECHNOLOGY
    • B82YSPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
    • B82Y40/00Manufacture or treatment of nanostructures
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D5/00Formation of filaments, threads, or the like
    • D01D5/06Wet spinning methods

Definitions

  • the present invention relates to conductive composite fibers comprising a polymeric matrix in which nano-sized graphene is dispersed. It also relates to processes for preparing these fibers, as well as their uses.
  • the electrically conductive fibers are known for different applications, making particular use of their antistatic properties, in particular for the manufacture of aeronautical or automotive parts or for the electromagnetic shielding of electronic equipment, for example to dissipate electrical charges arising from friction, induced in particular during the circulation of a fluid in a thermoplastic pipe. They can also be used in the manufacture of deformation or stress sensors.
  • the intrinsically conductive polymer fibers which are poorly resistant to washing and are not very stable, insofar as they are sensitive to oxidation and also to heat released by the Joule effect which can chemically degrade (for example crosslink) the polymer and / or alter its mechanical properties beyond a certain temperature,
  • the polymer fibers made conductive by deposition of conductive particles on their surface, such as silver fibers, whose coating is likely to degrade by friction and wear.
  • Composite fibers containing graphene are already known from WO 2010/107762 and US 2010/092723. These fibers are made from graphene obtained by graphite exfoliation and thus having a variable thickness depending on whether the exfoliation is more or less complete, and micrometric side dimensions. Commercially available exfoliation graphene grades have a length and width of more than 1 ⁇ m, typically 5, 15 or 25 ⁇ m and up to 50 ⁇ m.
  • the fibers described in these documents are obtained by molten route. However, this technique does not always make it possible to obtain fibers having a good electrical conductivity, insofar as it leads to an orientation of the charges such as graphene in the direction of the fiber, which is generally pred udiciables to the electrical properties. In addition, the molten process does not achieve high levels of graphene, given the high viscosity that they generate.
  • nanoscale graphene made it possible to prepare fibers having a high electrical conductivity and good mechanical properties. It is also possible to manufacture these fibers by a simple coagulation process to implement, under conditions of high productivity.
  • the subject of the present invention is thus conductive composite fibers containing graphene dispersed in a polymer matrix, characterized in that the graphene is in the form of particles having a thickness of less than 100 nm, preferably less than 50 nm. , more preferably less than 15 nm, between 0.1 and 10 nm, and lateral dimensions of about 1 ⁇ m, more preferably from 50 to 800 nm, more particularly from 100 to 600 nm, or even from 100 to 500 nm .
  • fiber is meant, in the sense of the present invention, a strand whose diameter is between 100 nm (nanometers) and 300 ⁇ (micrometers), preferably between 1 and 100 ⁇ (micrometers), better, between 2 and 50 ⁇ (micrometers).
  • This structure may also be porous or non-porous.
  • Graphene is a material discovered in 2004 and has since been manufactured on an industrial scale. It is a two-dimensional crystal made up of carbon atoms arranged in a honeycomb, the stack of which constitutes graphite (where 1 mm of graphite contains several million graphene sheets).
  • graphene is therefore used to designate a sheet of graphite plane, isolated and individualized, but also, by extension, an assembly comprising between one and a few tens of sheets and having a flat structure or more or less wavy .
  • This definition includes FLGs (Few Layer Graphene or Graphene NanoRegons), Nanosized Graphene Plates (NGPs), CNS (Carbon NanoSheets or nano-graphene sheets), and Graphene NanoRibbons (Graphene NanoRibbons). nano-ribbons of graphene). On the other hand, it excludes carbon nanotubes and nanofibers.
  • the graphene used according to the invention is in the form of particles having a thickness of less than 100 nm, preferably less than 50 nm, more preferably less than 15 nm, and lateral dimensions of approximately 1 ⁇ m, preferably from 50 to 800, more preferably still from 100 to 600 nm, or even from 100 to 500 nm.
  • Each of these particles generally contains from 1 to 50 sheets which are likely to be detached from one of the others in the form of independent leaflets, for example during an ultrasound treatment.
  • Graphene is advantageously prepared according to a chemical vapor deposition or "CVD" method.
  • Such a process generally comprises the decomposition of a gaseous source of carbon, in particular a hydrocarbon, such as ethylene, methane or acetylene, at a temperature of 800 to 1000 ° C., over a supported catalyst. in powder form, in particular on cobalt optionally mixed with iron and supported on magnesia.
  • a preferred CVD method for obtaining graphene according to this invention comprises the following steps:
  • step b) contacting a gaseous carbon source with the catalyst of step b), optionally in a fluidized bed, and its catalytic decomposition at a temperature of 500 to 800 ° C, preferably from 610 to 800 ° C, the gas source being selected from alcohols C 1 -C 1 2 and hydrocarbons C 1 -C 1 2, such as alkanes or alkenes, of preferably ethylene, which can be mixed with a flow of hydrogen as reducing agent and optionally with an inert gas,
  • the amount of graphene used according to the invention represents from 0.5% to 50%, preferably from 1% to 30%, more preferably from 3.5% to 15% by weight, relative to the total weight composite fiber.
  • the present invention also relates to processes for producing these conductive composite fibers by coagulation.
  • the coagulation process may include:
  • the composite fibers according to the invention can be produced by a process comprising the successive steps of:
  • the first step of the process according to the invention consists in forming a graphene dispersion in a binder polymer, in the presence of at least one stabilizing agent covalently or non-covalently bonded to graphene.
  • the binder polymer may be chosen from a homo- or copolymer of vinyl alcohol, cellulose, viscose, an alginate, poly (lactic acid), poly (lactic acid-co-glycolic acid), and mixtures thereof, particularly polyvinyl alcohol.
  • the term "stabilizing agent” is intended to mean a compound which allows a homogeneous dispersion of graphene in the solution, which protects graphene from coagulation in the presence of the polymeric binder, but which does not interfere with the coagulation of the polymeric binder in a coagulation solution.
  • the stabilizing agent (s) according to the invention are bonded to graphene either covalently or non-covalently.
  • the stabilizing agent is non-covalently bonded to graphene, it may be chosen from essentially nonionic surfactants.
  • substantially nonionic surfactant is meant, in the sense of the present invention, a nonionic amphiphilic compound, cited for example in the book McCUTCHEON'S 2008 "Emulsifiers and Detergents", and preferably having a HLB (hydrophilic-lipophilic balance) from 13 to 16, as well as block copolymers containing hydrophilic blocks and lipophilic blocks and having a low ionicity, for example 0% to 10% by weight of ionic monomer and 90% to 100% of nonionic monomer.
  • HLB hydrophilic-lipophilic balance
  • the stabilizing agent is covalently bonded to graphene
  • it is preferably a hydrophilic group, preferably a polyethylene glycol group grafted on graphene.
  • the grafting of reactive units such as polyethylene glycol groups on the surface of graphene can be carried out according to any method known to those skilled in the art.
  • one skilled in the art may disperse graphene in dimethylformamide (DMF) before contacting it with oxalyl chloride.
  • DMF dimethylformamide
  • PEG polyethylene glycol
  • the dispersion produced in the first step of the process according to the invention comprises a solvent which is preferably chosen from water, dimethylsulfoxide (DMSO), glycerol, ethylene glycol, diethylene glycol and triethylene glycol. , diethylene triamine, ethylene diamine, phenol, dimethylformamide (DMF), dimethylacetamide, N-methylpyrrolidone and mixtures thereof.
  • a solvent which is preferably chosen from water, dimethylsulfoxide (DMSO), glycerol, ethylene glycol, diethylene glycol and triethylene glycol. , diethylene triamine, ethylene diamine, phenol, dimethylformamide (DMF), dimethylacetamide, N-methylpyrrolidone and mixtures thereof.
  • the solvent is chosen from water, DMSO and mixtures thereof in all proportions.
  • the pH of the aqueous dispersion can be maintained preferably between 3 and 5 by addition of one or more acids, which can be chosen from inorganic acids, such as sulfuric acid, nitric acid and hydrochloric acid, organic acids such as acetic acid, tartaric acid and oxalic acid and mixtures of organic acid and organic acid salt such as acid citric acid and sodium citrate, acetic acid and sodium acetate, tartaric acid and potassium tartrate, tartaric acid and sodium citrate.
  • inorganic acids such as sulfuric acid, nitric acid and hydrochloric acid
  • organic acids such as acetic acid, tartaric acid and oxalic acid and mixtures of organic acid and organic acid salt such as acid citric acid and sodium citrate, acetic acid and sodium acetate, tartaric acid and potassium tartrate, tartaric acid and sodium citrate.
  • the dispersion may comprise boric acid, borate salts, or mixtures thereof.
  • the dispersion may also comprise a salt selected from zinc chloride, sodium thiocyanate, calcium chloride, aluminum chloride, lithium chloride, rhodanates and mixtures thereof. They make it possible to optimize the rheological properties of the dispersion and to promote the formation of the fiber.
  • the dispersion is carried out by means of ultrasound or a rotor-stator system or a ball mill. It can be carried out at room temperature, or by heating, for example, between 40 and 120 ° C.
  • the second step of the process involves injecting said dispersion obtained in the first step into a coagulation solution to form a fiber, in the form of monofilament or multi-filaments.
  • coagulation solution is intended to mean a solution which causes the polymer binder to solidify.
  • Such solutions are known to those skilled in the art, and the production of vinyl alcohol homo- or copolymer-based fibers is the subject of a rich literature.
  • wet spinning refer for example to US Patents 3,850,901, US 3,852,402 and US 4,612,157.
  • dry-jet wet spinning of PVA, or “dry-jet wet spinning” (refer, for example, to US Patents 4,603,083, US 4,698,194, US 4,971,861, US 5,208,104 and US Pat.
  • the coagulation solution comprises a solvent chosen from water, an alcohol, a polyol, a ketone and their mixtures, more preferably a solvent chosen from water, methanol, ethanol, butanol, propanol, isopropanol, glycol, acetone, methyl ethyl ketone, methyl isobutyl ketone, benzene, toluene and mixtures thereof, and still more more preferred a solvent selected from water, methanol, ethanol, a glycol, acetone and mixtures thereof.
  • the coagulation solution advantageously has a temperature of between 10 and 80 ° C. If the solvent of the coagulation solution is essentially organic, such as methanol, the coagulation solution advantageously has a temperature between -30 and 10 ° C.
  • the coagulation solution may comprise one or more salts intended to promote the coagulation of the polymeric binder, chosen from alkaline salts or desiccant salts such as ammonium sulphate, potassium sulphate, sodium sulphate, sodium carbonate, sodium hydroxide, potassium hydroxide and mixtures thereof.
  • alkaline salts or desiccant salts such as ammonium sulphate, potassium sulphate, sodium sulphate, sodium carbonate, sodium hydroxide, potassium hydroxide and mixtures thereof.
  • the coagulation solution may comprise one or more additional compounds which are intended to improve the mechanical properties, the water resistance of the fiber and / or facilitate the spinning of the fiber.
  • the coagulation solution can therefore comprise at least one compound selected from boric acid, borate salts and mixtures thereof.
  • the coagulation solution is saturated with salts.
  • the dispersion is injected during the second step of the process according to the invention through one or a set of needles and / or one or a set of nonporous cylindrical or conical nozzles into the coagulation solution, which can be static (static bath) or in motion (flow).
  • the average injection speed of the dispersion may be between 0.1 m / min and 50 m / min, preferably between 0.5 m / min and 20 m / min.
  • the coagulant solution induces coagulation in the form of a fiber by solidification of the polymeric binder. Graphene gets trapped in the polymer that solidifies.
  • the next step of the process according to the invention consists in extracting, continuously or not, the fiber from the coagulation solution.
  • the wash tank preferably includes water.
  • the washing step may make it possible to eliminate a portion of the peripheral polymer from the fiber and thus enrich the composition of the fiber with graphene.
  • the washing bath may include agents that alter the composition of the fiber or interact with each other. chemically with this one.
  • chemical or physical crosslinking agents in particular borate salts or dialdehydes, may be added to the bath in order to reinforce the fiber.
  • the washing step may also make it possible to eliminate the agents, in particular the surfactants, potentially pre-limpable to the mechanical or electrical properties of the fiber.
  • a drying step is also included in the process according to the invention. This step can take place either directly after extraction or after washing. In particular, if it is desired to obtain a polymer-enriched fiber, it is desirable to dry the fiber directly after the extraction.
  • the drying is preferably carried out in an oven which will dry the fiber by means of a gas circulating in an interior duct of the oven. The drying can also be carried out by infrared radiation.
  • the composite fibers according to the invention may be produced according to a process comprising the successive steps consisting of:
  • the composite fibers according to the invention can be produced according to a process comprising the successive steps consisting of:
  • a multilayer fiber is thus obtained containing: a core formed of a natural or synthetic fiber,
  • a bark containing a polymeric binder and graphene containing a polymeric binder and graphene.
  • the solvents, stabilizing agents, polymeric binders and coagulation solutions used in this process may be chosen from those mentioned above.
  • An example of such a process has been described in the application FR 2 946 178, to which reference may be made for further details.
  • they may include a winding step, and possibly a hot stretching step performed between the drying step and the winding step. They may also include stretches in solvents at different times.
  • composite fibers obtained by this method are intrinsically conductive, their electrical conductivity can be further improved by heat treatments.
  • the composite fibers according to the invention may comprise other conductive carbonaceous fillers in addition to graphene, in particular one or more fillers chosen from carbon nanotubes, nanofibres of carbon, and mixtures thereof.
  • Carbon nanofibers are, like carbon nanotubes, nanofilaments generally produced by chemical vapor deposition (or CVD) from a carbon source that is decomposed on a catalyst having a transition metal (Fe, Ni, Co, Cu) in the presence of hydrogen at temperatures of 500 to 1200 ° C.
  • CVD chemical vapor deposition
  • these two carbonaceous charges are differentiated by their structure (I. MARTIN-GULLON et al., Carbon, Vol 44, 1572-1580, 2006).
  • the carbon nanotubes consist of one or more sheets of graphene wound concentrically to form a cylinder having a diameter of 1 to 100 nm.
  • carbon nanofibers are composed of more or less organized graphitic zones (or turbostratic stacks) whose planes are inclined at variable angles with respect to the axis of the fiber. These stacks can take the form of platelets, fish bones or stacked cups to form structures generally ranging in diameter from 100 nm to 500 nm or more.
  • the carbon nanotubes that can be used in the present invention are advantageously of multi-wall type, containing from 5 to 15 walls, and are preferably obtained by a chemical vapor deposition (CVD) process. They advantageously have a mean diameter ranging from 0.1 to 100 nm and a length of 0.1 to 20 ⁇ m.
  • Examples of crude carbon nanotubes are those commercially available from ARKEMA under the trademark Graphistrength C100.
  • the fibers according to the invention may comprise an assembly of carbon and graphene nanotubes capable of being obtained by decomposition at a temperature of 500 to 1500 ° C. of a source of carbon in the gaseous state, implemented contact with an active catalyst A for the synthesis of carbon nanotubes and an active catalyst B for the synthesis of graphene.
  • This assembly can thus be obtained by adapting the graphene synthesis process described above to add catalyst A.
  • the latter may in particular comprise a metal such as iron, cobalt, nickel, molybdenum, titanium and mixtures thereof. supported on a solid inert support, for example alumina.
  • Such a catalyst may especially be prepared by impregnating a dry substrate with an aqueous or alcoholic impregnation solution comprising metal salts.
  • the composite fibers according to the invention may contain at least one conductive polymer.
  • conducting polymer is meant a homo- or copolymer whose main chain contains conjugated double bonds - for example in the form of one or more (hetero) aromatic rings - and which forms, after possible oxidation and doping with the using at least one doping agent, a salt or complex having electrical conduction properties.
  • usable conductive polymers include homo- and copolymers comprising one or more monomers selected from aniline, pyrrole, optionally substituted thiophene, acetylene, phenylene vinylene, phenylene sulfide and mixtures thereof.
  • PEDOT poly(3,4-ethylenedioxythiophene) or PEDOT.
  • PEDOT and PANI are preferred for use in the present invention.
  • Polyaniline exists under different oxidation states, related to the proportions of imine and amine functions contained in the molecule. It is preferred according to the invention to use emeraldine, which corresponds to the intermediate oxidation state of polyaniline, having the best electrical properties.
  • doping agents include strong protonic acids having a pKa of less than 3, such as hydrochloric acid, sulfuric acid and its salts such as sodium dodecyl sulphate, phosphonic acids and sulphonic compounds, especially 2-acrylamido-2-methylpropanesulphonic acid (AMPS), dodecylbenzenesulfonic acid, camphorsulfonic acid, toluenesulphonic acid, methanesulphonic acid and sulphonic function (s) polymers, such as that the poly (styrene sulfonic acid) which is the doping agent preferably used in combination with the PEDOT to form a colloidal solution PEDOT: PSS.
  • Other doping agents include polyacrylamide and polyacrylic acid.
  • the salts or complexes of conductive polymers and doping agents can be obtained chemically or electrochemically, according to techniques known to those skilled in the art. Some are also available commercially, especially from PANIPOL.
  • These conductive polymers can be incorporated in the composite fibers according to the invention in one of or the other of the variants described above, by mixing them with the polymeric binder before the coagulation step.
  • the present invention also relates to the use of the above-mentioned conductive composite fibers for the manufacture of nose, wings or cockles of rockets or airplanes; off-shore flexible armor; automotive bodywork components, engine chassis or automobile support parts; automotive seat coverings; structural elements in the field of buildings or bridges and roadways; packaging and antistatic textiles, in particular antistatic curtains, antistatic clothing (for example, safety or clean room) or materials for the protection of silos or the packaging and / or transport of powders or granular materials; furnishing items, including clean room furniture; filters; electromagnetic shielding devices, in particular for the protection of electronic components; conductive cables; sensors, in particular deformation sensors or mechanical stresses; electrodes; hydrogen storage devices; biomedical devices such as sutures, prostheses or catheters; displays, keyboards or connectors incorporated into clothing; or receivers and emitters of electromagnetic waves.
  • the manufacture of these composite parts can be carried out according to various processes, generally involving a step of impregnating the conductive composite fibers according to the invention with a composition polymeric material comprising at least one thermoplastic, elastomeric or thermosetting material.
  • This impregnation step may itself be carried out according to various techniques, depending in particular on the physical form of the polymeric composition used.
  • the impregnation of the conductive composite fibers is preferably carried out according to a fluidized bed impregnation process, in which the polymeric composition is in the form of powder. Pre-impregnated fibers are thus obtained.
  • preimpregnated fiber fabrics of identical or different composition, can be stacked to form a plate or a laminated material, or alternatively subjected to a thermoforming process.
  • the pre-impregnated fibers may be combined to form ribbons which may be used in a filament winding process which makes it possible to obtain hollow pieces of almost unlimited shape, by winding the ribbons on a mandrel having the shape of the part to be made.
  • the manufacture of the finished part comprises a step of consolidating the polymeric composition, which is for example melted locally to create zones for fixing the fibers pre-impregnated with each other and / or to secure the fiber ribbons pre-impregnated with each other. impregnated in the filament winding process.
  • the conductive composite fibers according to the invention can be woven or knitted, alone or with other fibers, or used, alone or in combination with other fibers, for the manufacture of cables, felts or nonwoven materials.
  • materials constituting these other fibers include, without limitation:
  • stretched polymer fibers based in particular on: polyamide such as polyamide 6 (PA-6), polyamide 11 (PA-11), polyamide 12 (PA-12), polyamide 6.6 (PA-6.6) the polyamide 4.6 (PA-4,6), polyamide-6,10 (PA-6.10) or polyamide 6.12 (PA-6.12), copolymer polyamide / polyether block (Pebax ®), high density polyethylene, polypropylene or polyester such as polyhydroxyalkanoates and polyesters marketed by Du Pont under the trade name Hytrel ®;
  • glass fibers especially of type E, R or
  • Step 1 Synthesis of assemblages of carbon nanotubes and graphene (NTC / GP)
  • the homogeneous gel thus obtained was heated to a temperature of the order of 200 ° C. so as to decompose citric acid. The expansion of the homogeneous gel was then observed to foam which was allowed to develop for about 30 minutes until stabilization. This foam was then crushed gently to form a powder which was heated at 400 ° C for 4 hours in atmospheric air. A crystalline powder of cobalt ferrite was thus obtained.
  • This powder had a single oxide phase having a spinel type structure with a crystalline domain size of between 14 nm and 20 nm (determined by X-ray diffraction) and a specific surface area of 7 m 2 / g.
  • a catalyst was prepared from Puralox ® SCCa-5/150 alumina with a median diameter of approximately 85 ⁇ and a specific surface area of 160 m 2 / g.
  • 100 g of alumina was introduced and flushed with air.
  • 80 ml of a 45 g / l solution of ammonium molybdate tetrahydrate were then continuously injected, followed by 560 ml of a 675 g / l solution of iron nitrate nonahydrate.
  • the target ratio (metal mass / catalyst mass) being 32% for iron and 3% for molybdenum, the duration of addition was 25 h.
  • the catalyst was then heated in situ at 220 ° C under dry air for 8 hours and then placed in a muffle furnace at 400 ° C for 8 hours.
  • a catalytic test was carried out by putting a mass of about 1.9 g of catalyst A and about 0.6 g catalyst B in a quartz reactor of 5 cm in diameter and 1 meter effective heating height.
  • the amount of product recovered at the end of the reaction was 47 g.
  • the theoretical NTC / GP mass ratio in this test was 90/10.
  • Step 2 Production of Composite Fibers Three aqueous dispersions were carried out, respectively from the two aforementioned assemblies and from NTC without graphene. To this was charged in water 0.9% by weight of the aforementioned charges and 1.2% by weight of a surfactant (Brij ® 78). These suspensions were then passed to the ultrasound microprobe for
  • Fibers that do not contain graphene have an electrical resistance greater than the detection threshold of the device used (Keithley ® 2000 multimeter), due to the orientation of the NTC along the fiber, which is unfavorable to the transmission of the current.
  • graphene-containing fibers have satisfactory electrical conductivity, which could be further enhanced by heat treatment.

Abstract

Graphene-based conductive composite fibres. The present invention relates to conductive composite fibre containing a polymer matrix in which nanometer-scale graphene is dispersed. It also relates to processes for preparing these fibres, and also to the uses thereof.

Description

Fibres composites conductrices à base de graphène  Graphene-based conductive composite fibers
La présente invention concerne des fibres composites conductrices renfermant une matrice polymérique dans laquelle est dispersé du graphène de taille nanométrique . Elle concerne également des procédés de préparation de ces fibres, ainsi que leurs utilisations. The present invention relates to conductive composite fibers comprising a polymeric matrix in which nano-sized graphene is dispersed. It also relates to processes for preparing these fibers, as well as their uses.
Les fibres conductrices de l'électricité sont connues pour différentes applications, mettant en particulier à profit leurs propriétés antistatiques, notamment pour la fabrication de pièces aéronautiques ou automobiles ou pour le blindage électromagnétique d'équipements électroniques, par exemple pour dissiper les charges électriques issues de frottements, induites en particulier lors de la circulation d'un fluide dans une conduite thermoplastique. Elles peuvent en outre être utilisées dans la fabrication de capteurs de déformations ou de contraintes. The electrically conductive fibers are known for different applications, making particular use of their antistatic properties, in particular for the manufacture of aeronautical or automotive parts or for the electromagnetic shielding of electronic equipment, for example to dissipate electrical charges arising from friction, induced in particular during the circulation of a fluid in a thermoplastic pipe. They can also be used in the manufacture of deformation or stress sensors.
Les fibres conductrices connues dans l'art antérieur comprennent : The conductive fibers known in the prior art include:
- les fils métalliques, qui ont l'inconvénient d'être lourds et susceptibles de s'oxyder,  metallic wires, which have the disadvantage of being heavy and liable to oxidize,
- les fibres de polymères intrinsèquement conducteurs, qui résistent mal aux lavages et sont peu stables, dans la mesure où ils sont sensibles à l'oxydation et également à la chaleur dégagée par effet Joule qui peut dégrader chimiquement (par exemple réticuler) le polymère et/ou altérer ses propriétés mécaniques au-delà d'une certaine température,  the intrinsically conductive polymer fibers, which are poorly resistant to washing and are not very stable, insofar as they are sensitive to oxidation and also to heat released by the Joule effect which can chemically degrade (for example crosslink) the polymer and / or alter its mechanical properties beyond a certain temperature,
- les fibres de polymères rendus conducteurs par dépôt de particules conductrices à leur surface, telles que les fibres argentées, dont le revêtement est susceptible de se dégrader par frottement et usure. the polymer fibers made conductive by deposition of conductive particles on their surface, such as silver fibers, whose coating is likely to degrade by friction and wear.
Il subsiste donc le besoin de disposer de nouvelles fibres conductrices présentant une conductivité électrique satisfaisante sans générer une quantité de chaleur trop forte, qui serait susceptible de dégrader la matrice de ces fibres. II serait par ailleurs souhaitable que ces fibres présentent d'autres propriétés avantageuses, en particulier qu'elles soient légères et/ou stables chimiquement et/ou qu'elles présentent une bonne tenue mécanique . There remains therefore the need to have new conductive fibers having a satisfactory electrical conductivity without generating too much heat, which would be likely to degrade the matrix of these fibers. It would also be desirable for these fibers to have other advantageous properties, in particular that they are light and / or chemically stable and / or that they have good mechanical strength.
Dans ce contexte, il est apparu aux inventeurs qu'il était possible de satisfaire ces besoins en proposant une fibre à base de graphène dispersé dans une matrice polymérique . In this context, it appeared to the inventors that it was possible to meet these needs by proposing a graphene-based fiber dispersed in a polymeric matrix.
Des fibres composites contenant du graphène sont déjà connues des documents WO 2010/107762 et US 2010/092723. Ces fibres sont fabriquées à partir de graphène obtenu par exfoliation de graphite et présentant, de ce fait, une épaisseur variable suivant que 1 ' exfoliâtion est plus ou moins complète, et des dimensions latérales micrométriques. Les grades de graphène obtenu par exfoliation disponibles dans le commerce présentent en effet une longueur et une largeur de plus de 1 pm, typiquement de 5, 15 ou 25 pm et allant jusqu'à 50 pm. En outre, les fibres décrites dans ces documents sont obtenues par voie fondue. Or, cette technique ne permet pas toujours d'obtenir des fibres présentant une bonne conductivité électrique, dans la mesure où elle conduit à une orientation des charges telles que le graphène dans le sens de la fibre, qui est généralement pré udiciables aux propriétés électriques. En outre, le procédé par voie fondue ne permet pas d'atteindre des teneurs en graphène élevées, compte tenu de la trop forte viscosité que celles-ci engendrent. Composite fibers containing graphene are already known from WO 2010/107762 and US 2010/092723. These fibers are made from graphene obtained by graphite exfoliation and thus having a variable thickness depending on whether the exfoliation is more or less complete, and micrometric side dimensions. Commercially available exfoliation graphene grades have a length and width of more than 1 μm, typically 5, 15 or 25 μm and up to 50 μm. In addition, the fibers described in these documents are obtained by molten route. However, this technique does not always make it possible to obtain fibers having a good electrical conductivity, insofar as it leads to an orientation of the charges such as graphene in the direction of the fiber, which is generally pred udiciables to the electrical properties. In addition, the molten process does not achieve high levels of graphene, given the high viscosity that they generate.
Or, il est apparu aux inventeurs que l'utilisation de graphène nanométrique permettait de préparer des fibres présentant une conductivité électrique élevée et de bonnes propriétés mécaniques. Il est également possible de fabriquer ces fibres suivant un procédé de coagulation simple à mettre en œuvre, dans des conditions de productivité élevée. Now, the inventors have discovered that the use of nanoscale graphene made it possible to prepare fibers having a high electrical conductivity and good mechanical properties. It is also possible to manufacture these fibers by a simple coagulation process to implement, under conditions of high productivity.
La présente invention a ainsi pour objet des fibres composites conductrices, renfermant du graphène dispersé dans une matrice polymérique, caractérisées en ce que le graphène se présente sous forme de particules d'une épaisseur de moins de 100 nm, de préférence de moins de 50 nm, plus préfèrentiellement de moins de 15 nm, comprise entre 0,1 et 10 nm, et de dimensions latérales d'environ 1 pm, plus préfèrentiellement de 50 à 800 nm, plus particulièrement de 100 à 600 nm, voire de 100 à 500 nm . The subject of the present invention is thus conductive composite fibers containing graphene dispersed in a polymer matrix, characterized in that the graphene is in the form of particles having a thickness of less than 100 nm, preferably less than 50 nm. , more preferably less than 15 nm, between 0.1 and 10 nm, and lateral dimensions of about 1 μm, more preferably from 50 to 800 nm, more particularly from 100 to 600 nm, or even from 100 to 500 nm .
Par « fibre », on entend, au sens de la présente invention, un brin dont le diamètre est compris entre 100 nm (nanomètres) et 300 μιη (micromètres), de préférence entre 1 et 100 μιη (micromètres), mieux, entre 2 et 50 μιη (micromètres) . Cette structure peut par ailleurs être ou non poreuse. Le graphène est un matériau découvert en 2004 et fabriqué depuis à l'échelle industrielle. Il s'agit d'un cristal bidimensionnel constitué d'atomes de carbone disposés en nid d'abeille, dont l'empilement constitue le graphite (où 1 mm de graphite renferme plusieurs millions de feuilles de graphène) . L'enroulement d'un ou plusieurs feuillets de graphène de manière coaxiale donne naissance aux nanotubes de carbone (respectivement, mono-parois et multi-parois ) , tandis que l'empilement turbostratique de ces feuillets constitue une nanofibre de carbone. Dans cette description, le terme « graphène » est donc utilisé pour désigner un feuillet de graphite plan, isolé et individualisé, mais aussi, par extension, un assemblage comprenant entre un et quelques dizaines de feuillets et présentant une structure plane ou plus ou moins ondulée. Cette définition englobe ainsi les FLG (Few Layer Graphene ou graphène faiblement empilé) , les NGP (Nanosized Graphene Plates ou plaques de graphène de dimension nanométrique ) , les CNS (Carbon NanoSheets ou nano-feuilles de graphène) , les GNR (Graphene NanoRibbons ou nano-rubans de graphène) . Elle exclut en revanche les nanotubes et nanofibres de carbone. Comme indiqué précédemment, le graphène utilisé selon l'invention se présente sous forme de particules d'une épaisseur de moins de 100 nm, de préférence de moins de 50 nm, plus préfèrentiellement de moins de 15 nm, et de dimensions latérales d'environ 1 pm, préfèrentiellement de 50 à 800, plus préfèrentiellement encore de 100 à 600 nm, voire de 100 à 500 nm. Chacune de ces particules renferme en général de 1 à 50 feuillets qui sont susceptibles d'être désolidarisés les uns des autres sous la forme de feuillets indépendants, par exemple lors d'un traitement par ultrasons. By "fiber" is meant, in the sense of the present invention, a strand whose diameter is between 100 nm (nanometers) and 300 μιη (micrometers), preferably between 1 and 100 μιη (micrometers), better, between 2 and 50 μιη (micrometers). This structure may also be porous or non-porous. Graphene is a material discovered in 2004 and has since been manufactured on an industrial scale. It is a two-dimensional crystal made up of carbon atoms arranged in a honeycomb, the stack of which constitutes graphite (where 1 mm of graphite contains several million graphene sheets). The winding of one or more sheets of graphene coaxially gives rise to the carbon nanotubes (respectively, single-wall and multi-wall), while the turbostratic stack of these sheets is a carbon nanofiber. In this description, the term "graphene" is therefore used to designate a sheet of graphite plane, isolated and individualized, but also, by extension, an assembly comprising between one and a few tens of sheets and having a flat structure or more or less wavy . This definition includes FLGs (Few Layer Graphene or Graphene NanoRegons), Nanosized Graphene Plates (NGPs), CNS (Carbon NanoSheets or nano-graphene sheets), and Graphene NanoRibbons (Graphene NanoRibbons). nano-ribbons of graphene). On the other hand, it excludes carbon nanotubes and nanofibers. As indicated above, the graphene used according to the invention is in the form of particles having a thickness of less than 100 nm, preferably less than 50 nm, more preferably less than 15 nm, and lateral dimensions of approximately 1 μm, preferably from 50 to 800, more preferably still from 100 to 600 nm, or even from 100 to 500 nm. Each of these particles generally contains from 1 to 50 sheets which are likely to be detached from one of the others in the form of independent leaflets, for example during an ultrasound treatment.
Le graphène est avantageusement préparé suivant un procédé de dépôt chimique en phase vapeur ou « CVD ». Un tel procédé comprend en général la décomposition d'une source gazeuse de carbone, en particulier un hydrocarbure, tel que de l'éthylène, du méthane ou de l'acétylène, à une température de 800 à 1000°C, sur un catalyseur supporté sous forme de poudre, notamment sur du cobalt éventuellement mélangé à du fer et supporté sur de la magnésie. Graphene is advantageously prepared according to a chemical vapor deposition or "CVD" method. Such a process generally comprises the decomposition of a gaseous source of carbon, in particular a hydrocarbon, such as ethylene, methane or acetylene, at a temperature of 800 to 1000 ° C., over a supported catalyst. in powder form, in particular on cobalt optionally mixed with iron and supported on magnesia.
Un procédé de CVD préféré pour l'obtention de graphène selon cette invention comprend les étapes suivantes : A preferred CVD method for obtaining graphene according to this invention comprises the following steps:
a) l'introduction dans un réacteur de synthèse, et éventuellement la mise en lit fluidisé dans ledit réacteur, d'un catalyseur actif pour la synthèse de graphène, tel qu'un oxyde mixte de formule AFe2Û4 où A est un élément métallique à valence mixte présentant au moins deux valences dont l'une est égale à +2, en particulier choisi parmi le cobalt, le cuivre ou le nickel, le catalyseur étant avantageusement de structure spinelle, b) le chauffage dudit catalyseur dans le réacteur, à une température comprise entre 500 et 1500°C, de préférence entre 500 et 800°C, voire entre 610 et 800°C, a) the introduction into a synthesis reactor, and optionally the fluidized bed in said reactor, of an active catalyst for the synthesis of graphene, such as a mixed oxide of formula AFe 2 O 4 where A is an element mixed valence metal having at least two valences of which one is +2, in particular selected from cobalt, copper or nickel, the catalyst being advantageously of spinel structure, b) heating said catalyst in the reactor, at a temperature between 500 and 1500 ° C, preferably between 500 and 800 ° C, or even between 610 and 800 ° C,
c) la mise en contact d'une source gazeuse de carbone avec le catalyseur de l'étape b) , éventuellement en lit fluidisé, et sa décomposition catalytique à une température de 500 à 800°C, de préférence de 610 à 800°C, la source gazeuse étant choisie parmi les alcools en C1-C12 et les hydrocarbures en C1-C12, tels que les alcanes ou les alcènes, de préférence l'éthylène, qui peut être mélangé à un flux d'hydrogène comme agent réducteur et éventuellement à un gaz inerte, c) contacting a gaseous carbon source with the catalyst of step b), optionally in a fluidized bed, and its catalytic decomposition at a temperature of 500 to 800 ° C, preferably from 610 to 800 ° C, the gas source being selected from alcohols C 1 -C 1 2 and hydrocarbons C 1 -C 1 2, such as alkanes or alkenes, of preferably ethylene, which can be mixed with a flow of hydrogen as reducing agent and optionally with an inert gas,
d) la récupération du graphène produit en c) en sortie du réacteur.  d) the recovery of graphene produced in c) at the outlet of the reactor.
La quantité de graphène mise en œuvre selon l'invention représente de 0,5 % à 50 %, de préférence de 1 % à 30 %, de façon plus préférée de 3,5 % à 15 % en poids, par rapport au poids total de la fibre composite. The amount of graphene used according to the invention represents from 0.5% to 50%, preferably from 1% to 30%, more preferably from 3.5% to 15% by weight, relative to the total weight composite fiber.
La présente invention a également pour objet des procédés de fabrication de ces fibres composites conductrices par coagulation. Le procédé de coagulation peut comprendre : The present invention also relates to processes for producing these conductive composite fibers by coagulation. The coagulation process may include:
- soit la coagulation sous forme de fibre, ou autour d'une fibre pré-formée, d'un mélange de graphène et de liant polymère, généralement le poly (alcool vinylique) , en le faisant passer dans une solution de coagulation,  either coagulation in the form of a fiber, or around a pre-formed fiber, a mixture of graphene and a polymeric binder, generally polyvinyl alcohol, by passing it through a coagulation solution,
- soit l'injection du graphène dispersé dans un solvant dans un co-écoulement d'une solution de coagulation renfermant un liant polymère tel que le poly(alcool vinylique).  or injection of graphene dispersed in a solvent in a co-flow of a coagulation solution containing a polymeric binder such as polyvinyl alcohol.
Ainsi, selon un premier mode de réalisation, les fibres composites selon l'invention peuvent être produites suivant un procédé comprenant les étapes successives consistant en : Thus, according to a first embodiment, the composite fibers according to the invention can be produced by a process comprising the successive steps of:
a) la formation d'une dispersion de graphène dans une solution de liant polymère, en présence d'au moins un agent stabilisant lié de façon covalente ou non covalente au graphène,  a) forming a graphene dispersion in a polymer binder solution, in the presence of at least one stabilizing agent covalently or non-covalently bound to graphene,
b) l'injection de ladite dispersion dans une solution de coagulation,  b) injecting said dispersion into a coagulation solution,
c) l'extraction de la fibre obtenue,  c) extracting the obtained fiber,
d) le lavage éventuel de ladite fibre,  d) the possible washing of said fiber,
e) le séchage de ladite fibre.  e) drying said fiber.
Un tel procédé a été décrit en détail dans la demande FR 2 946 177 à laquelle on pourra se reporter pour plus de détails. Such a method has been described in detail in application FR 2 946 177 to which reference may be made for more details.
La première étape du procédé selon l'invention consiste à former une dispersion de graphène dans un polymère liant, en présence d'au moins un agent stabilisant lié de façon covalente ou non covalente au graphène . The first step of the process according to the invention consists in forming a graphene dispersion in a binder polymer, in the presence of at least one stabilizing agent covalently or non-covalently bonded to graphene.
Le polymère liant peut être choisi parmi un homo- ou copolymère d'alcool vinylique, la cellulose, la viscose, un alginate, le poly (acide lactique), le poly (acide lactique-co-acide glycolique) , et leurs mélanges, en particulier le poly(alcool vinylique. The binder polymer may be chosen from a homo- or copolymer of vinyl alcohol, cellulose, viscose, an alginate, poly (lactic acid), poly (lactic acid-co-glycolic acid), and mixtures thereof, particularly polyvinyl alcohol.
Par « agent stabilisant », on entend au sens de la présente invention, un composé permettant une dispersion homogène du graphène dans la solution, qui protège le graphène de la coagulation en présence du liant polymère, mais qui n'entrave pas la coagulation du liant polymère dans une solution de coagulation. For the purpose of the present invention, the term "stabilizing agent" is intended to mean a compound which allows a homogeneous dispersion of graphene in the solution, which protects graphene from coagulation in the presence of the polymeric binder, but which does not interfere with the coagulation of the polymeric binder in a coagulation solution.
Le ou les agent (s) stabilisant ( s ) selon l'invention sont liés au graphène soit de façon covalente, soit de façon non covalente. The stabilizing agent (s) according to the invention are bonded to graphene either covalently or non-covalently.
Dans le cas où l'agent stabilisant est lié au graphène de façon non covalente, il pourra être choisi parmi les tensioactifs essentiellement non ioniques. In the case where the stabilizing agent is non-covalently bonded to graphene, it may be chosen from essentially nonionic surfactants.
Par « tensioactif essentiellement non ionique » on entend, au sens de la présente invention, un composé amphiphile non ionique, cité par exemple dans l'ouvrage McCUTCHEON'S 2008 « Emulsifiers and Détergents », et ayant de préférence une HLB (balance hydrophile- lipophile) de 13 à 16, ainsi que les copolymères blocs renfermant des blocs hydrophiles et des blocs lipophiles et présentant une ionicité faible, par exemple 0% à 10% en poids de monomère ionique et 90% à 100% de monomère non ionique. By "substantially nonionic surfactant" is meant, in the sense of the present invention, a nonionic amphiphilic compound, cited for example in the book McCUTCHEON'S 2008 "Emulsifiers and Detergents", and preferably having a HLB (hydrophilic-lipophilic balance) from 13 to 16, as well as block copolymers containing hydrophilic blocks and lipophilic blocks and having a low ionicity, for example 0% to 10% by weight of ionic monomer and 90% to 100% of nonionic monomer.
Dans le second cas où l'agent stabilisant est lié au graphène de façon covalente, il s'agit de préférence d'un groupement hydrophile, avantageusement d'un groupement polyéthylèneglycol greffé sur le graphène. In the second case where the stabilizing agent is covalently bonded to graphene, it is preferably a hydrophilic group, preferably a polyethylene glycol group grafted on graphene.
Le greffage de motifs réactifs tels que des groupements polyéthylèneglycol à la surface du graphène peut être réalisé selon tout procédé connu de l'homme du métier. Par exemple, l'homme du métier pourra disperser le graphène dans du diméthylformamide (DMF) avant de le mettre en contact avec du chlorure d'oxalyle. Dans un second temps, la dispersion obtenue sera mise en contact avec du polyéthylène glycol (PEG) . The grafting of reactive units such as polyethylene glycol groups on the surface of graphene can be carried out according to any method known to those skilled in the art. For example, one skilled in the art may disperse graphene in dimethylformamide (DMF) before contacting it with oxalyl chloride. In one second time, the resulting dispersion will be contacted with polyethylene glycol (PEG).
En outre, la dispersion réalisée dans la première étape du procédé selon l'invention comprend un solvant qui est de préférence choisi parmi l'eau, le diméthylsulfoxyde (DMSO) , la glycérine, l'éthylène glycol, le diéthylène glycol, le triéthylène glycol, la diéthylène triamine, l'éthylène diamine, le phénol, le diméthylformamide (DMF) , le diméthylacétamide, la N- méthylpyrrolidone et leurs mélanges. De manière préférée, le solvant est choisi parmi l'eau, le DMSO et leurs mélanges en toutes proportions. In addition, the dispersion produced in the first step of the process according to the invention comprises a solvent which is preferably chosen from water, dimethylsulfoxide (DMSO), glycerol, ethylene glycol, diethylene glycol and triethylene glycol. , diethylene triamine, ethylene diamine, phenol, dimethylformamide (DMF), dimethylacetamide, N-methylpyrrolidone and mixtures thereof. Preferably, the solvent is chosen from water, DMSO and mixtures thereof in all proportions.
S'il s'agit d'une dispersion aqueuse, le pH de la dispersion aqueuse peut être maintenu de préférence entre 3 et 5 par ajout d'un ou de plusieurs acides, pouvant être choisis parmi les acides inorganiques, tels que l'acide sulfurique, l'acide nitrique et l'acide hydrochlorique, les acides organiques tels que l'acide acétique, l'acide tartrique et l'acide oxalique et les mélanges d'acide organique et de sel d'acide organique tels que l'acide citrique et le citrate de sodium, l'acide acétique et l'acétate de sodium, l'acide tartrique et le tartrate de potassium, l'acide tartrique et le citrate de sodium. If it is an aqueous dispersion, the pH of the aqueous dispersion can be maintained preferably between 3 and 5 by addition of one or more acids, which can be chosen from inorganic acids, such as sulfuric acid, nitric acid and hydrochloric acid, organic acids such as acetic acid, tartaric acid and oxalic acid and mixtures of organic acid and organic acid salt such as acid citric acid and sodium citrate, acetic acid and sodium acetate, tartaric acid and potassium tartrate, tartaric acid and sodium citrate.
D'autre part, la dispersion peut comprendre de l'acide borique, des sels de borate ou leurs mélanges. On the other hand, the dispersion may comprise boric acid, borate salts, or mixtures thereof.
En outre, la dispersion peut aussi comprendre un sel choisi parmi le chlorure de zinc, le thiocyanate de sodium, le chlorure de calcium, le chlorure d'aluminium, le chlorure de lithium, les rhodanates et leurs mélanges. Ils permettent d'optimiser les propriétés rhéologiques de la dispersion et de favoriser la formation de la fibre. In addition, the dispersion may also comprise a salt selected from zinc chloride, sodium thiocyanate, calcium chloride, aluminum chloride, lithium chloride, rhodanates and mixtures thereof. They make it possible to optimize the rheological properties of the dispersion and to promote the formation of the fiber.
Selon une forme avantageuse de la présente invention, la dispersion est réalisée au moyen d'ultrasons ou d'un système rotor-stator ou d'un broyeur à billes. Elle peut être réalisée à température ambiante, ou bien en chauffant, par exemple, entre 40 et 120°C. According to an advantageous form of the present invention, the dispersion is carried out by means of ultrasound or a rotor-stator system or a ball mill. It can be carried out at room temperature, or by heating, for example, between 40 and 120 ° C.
La deuxième étape du procédé consiste à injecter ladite dispersion obtenue lors de la première étape dans une solution de coagulation pour former une fibre, sous forme de mono-filament ou de multi-filaments . The second step of the process involves injecting said dispersion obtained in the first step into a coagulation solution to form a fiber, in the form of monofilament or multi-filaments.
Par « solution de coagulation », on entend au sens de la présente invention une solution qui provoque la solidification du liant polymère. De telles solutions sont connues de l'homme du métier, et la production de fibres à base d'homo- ou copolymère d'alcool vinylique fait l'objet d'une littérature riche. De manière générale, les techniques les plus courantes sont le filage au mouillé du PVA, ou « wet spinning » (terminologie anglo-saxonne ; se référer par exemple aux brevets US 3 850 901, US 3 852 402 et US 4 612 157) et le filage au mouillé à jet sec du PVA, ou « dry-jet wet spinning » (terminologie anglo-saxonne ; se référer par exemple aux brevets US 4 603 083, US 4 698 194, US 4 971 861, US 5 208 104 etFor the purposes of the present invention, the term "coagulation solution" is intended to mean a solution which causes the polymer binder to solidify. Such solutions are known to those skilled in the art, and the production of vinyl alcohol homo- or copolymer-based fibers is the subject of a rich literature. In general, the most common techniques are the wet spinning of PVA, or "wet spinning", refer for example to US Patents 3,850,901, US 3,852,402 and US 4,612,157). dry-jet wet spinning of PVA, or "dry-jet wet spinning" (refer, for example, to US Patents 4,603,083, US 4,698,194, US 4,971,861, US 5,208,104 and US Pat.
US 7 026 049) . Selon une forme avantageuse d'exécution de la présente invention, la solution de coagulation comprend un solvant choisi parmi l'eau, un alcool, un polyol, une cétone et leurs mélanges, de manière plus préférée un solvant choisi parmi l'eau, le méthanol, l'éthanol, le butanol, le propanol, 1 ' isopropanol , un glycol, l'acétone, le méthyl-éthyl-cétone, le méthyl-isobutyl- cétone, le benzène, le toluène et leurs mélanges, et de manière encore plus préférée un solvant choisi parmi l'eau, le méthanol, l'éthanol, un glycol, l'acétone et leurs mélanges. US 7,026,049). According to an advantageous embodiment of the present invention, the coagulation solution comprises a solvent chosen from water, an alcohol, a polyol, a ketone and their mixtures, more preferably a solvent chosen from water, methanol, ethanol, butanol, propanol, isopropanol, glycol, acetone, methyl ethyl ketone, methyl isobutyl ketone, benzene, toluene and mixtures thereof, and still more more preferred a solvent selected from water, methanol, ethanol, a glycol, acetone and mixtures thereof.
Si le solvant de la solution de coagulation est essentiellement de l'eau, la solution de coagulation a de manière avantageuse une température comprise entre 10 et 80°C. Si le solvant de la solution de coagulation est essentiellement organique, tel que le méthanol, la solution de coagulation a de manière avantageuse une température comprise entre -30 et 10°C. If the solvent of the coagulation solution is essentially water, the coagulation solution advantageously has a temperature of between 10 and 80 ° C. If the solvent of the coagulation solution is essentially organic, such as methanol, the coagulation solution advantageously has a temperature between -30 and 10 ° C.
En outre, la solution de coagulation peut comprendre un ou plusieurs sels destinés à favoriser la coagulation du liant polymère, choisis parmi les sels alcalins ou les sels déshydratants tels que le sulfate d'ammonium, le sulfate de potassium, le sulfate de sodium, le carbonate de sodium, l'hydroxyde de sodium, l'hydroxyde de potassium et leurs mélanges. In addition, the coagulation solution may comprise one or more salts intended to promote the coagulation of the polymeric binder, chosen from alkaline salts or desiccant salts such as ammonium sulphate, potassium sulphate, sodium sulphate, sodium carbonate, sodium hydroxide, potassium hydroxide and mixtures thereof.
D'autre part, la solution de coagulation peut comprendre un ou plusieurs composés additionnels qui sont destinés à améliorer les propriétés mécaniques, la résistance à l'eau de la fibre et/ou à faciliter le filage de la fibre. La solution de coagulation peut donc comprendre au moins un composé choisi parmi l'acide borique, les sels de borate et leurs mélanges. On the other hand, the coagulation solution may comprise one or more additional compounds which are intended to improve the mechanical properties, the water resistance of the fiber and / or facilitate the spinning of the fiber. The coagulation solution can therefore comprise at least one compound selected from boric acid, borate salts and mixtures thereof.
De préférence, la solution de coagulation est saturée en sels. Preferably, the coagulation solution is saturated with salts.
De manière avantageuse, la dispersion est injectée lors de la deuxième étape du procédé selon l'invention à travers une ou un ensemble d'aiguilles et/ou une ou un ensemble de buses cylindriques ou coniques non poreuses dans la solution de coagulation, qui peut être statique (bain statique) ou en mouvement (écoulement) . La vitesse moyenne d'injection de la dispersion peut être comprise entre 0,1 m/min et 50 m/min, de préférence comprise entre 0,5 m/min et 20 m/min. Advantageously, the dispersion is injected during the second step of the process according to the invention through one or a set of needles and / or one or a set of nonporous cylindrical or conical nozzles into the coagulation solution, which can be static (static bath) or in motion (flow). The average injection speed of the dispersion may be between 0.1 m / min and 50 m / min, preferably between 0.5 m / min and 20 m / min.
La solution coagulante induit la coagulation sous forme d'une fibre par solidification du liant polymère. Le graphène se retrouve piégé dans le polymère qui se solidifie. The coagulant solution induces coagulation in the form of a fiber by solidification of the polymeric binder. Graphene gets trapped in the polymer that solidifies.
L'étape suivante du procédé selon l'invention consiste à extraire, de manière continue ou non, la fibre de la solution de coagulation. The next step of the process according to the invention consists in extracting, continuously or not, the fiber from the coagulation solution.
Après l'extraction de la fibre, celle-ci peut être éventuellement lavée une ou plusieurs fois. Le bac de lavage comprend préférablement de l'eau. L'étape de lavage peut permettre d'éliminer une partie du polymère périphérique de la fibre et ainsi d'enrichir la composition de la fibre en graphène. En outre, le bain de lavage peut comprendre des agents qui permettent de modifier la composition de la fibre ou qui interagissent chimiquement avec celle-ci. Notamment, des agents de réticulation chimique ou physique, en particulier des sels de borate ou des dialdéhydes, peuvent être ajoutés au bain afin de renforcer la fibre. L'étape de lavage peut aussi permettre d'éliminer les agents, notamment les tensioactifs, potentiellement pré udiciables aux propriétés mécaniques ou électriques de la fibre. After extraction of the fiber, it may be washed once or several times. The wash tank preferably includes water. The washing step may make it possible to eliminate a portion of the peripheral polymer from the fiber and thus enrich the composition of the fiber with graphene. In addition, the washing bath may include agents that alter the composition of the fiber or interact with each other. chemically with this one. In particular, chemical or physical crosslinking agents, in particular borate salts or dialdehydes, may be added to the bath in order to reinforce the fiber. The washing step may also make it possible to eliminate the agents, in particular the surfactants, potentially pre-limpable to the mechanical or electrical properties of the fiber.
Une étape de séchage est également comprise dans le procédé selon l'invention. Cette étape peut avoir lieu soit directement après l'extraction, soit consécutivement au lavage. Notamment, si on souhaite obtenir une fibre enrichie en polymère, il est souhaitable de sécher la fibre directement après l'extraction. Le séchage est de préférence réalisé dans un four qui va sécher la fibre grâce à un gaz circulant dans un conduit intérieur du four. Le séchage peut aussi être réalisé par rayonnement infrarouge . Selon un second mode de réalisation, les fibres composites selon l'invention peuvent être produites suivant un procédé comprenant les étapes successives consistant en : A drying step is also included in the process according to the invention. This step can take place either directly after extraction or after washing. In particular, if it is desired to obtain a polymer-enriched fiber, it is desirable to dry the fiber directly after the extraction. The drying is preferably carried out in an oven which will dry the fiber by means of a gas circulating in an interior duct of the oven. The drying can also be carried out by infrared radiation. According to a second embodiment, the composite fibers according to the invention may be produced according to a process comprising the successive steps consisting of:
la dispersion de graphène dans un solvant à l'aide éventuellement d'un agent tensioactif,  the dispersion of graphene in a solvent possibly using a surfactant,
l'injection de la dispersion de graphène dans un co- écoulement d'une solution de coagulation renfermant un liant polymère,  injecting the graphene dispersion into a co-flow of a coagulation solution containing a polymeric binder,
l'extraction de la fibre obtenue,  extraction of the obtained fiber,
- le lavage éventuel de ladite fibre, et the eventual washing of said fiber, and
le séchage de ladite fibre. Les solvants, tensioactifs, solutions de coagulation et liants polymères peuvent être choisis parmi ceux cités précédemment . Pour une description plus précise de ce procédé, on pourra se référer à la demande FR 2 921 075. drying said fiber. The solvents, surfactants, coagulation solutions and polymeric binders may be chosen from those mentioned above. For a more precise description of this process, reference may be made to application FR 2 921 075.
Selon un troisième mode de réalisation, les fibres composites selon l'invention peuvent être produites suivant un procédé comprenant les étapes successives consistant en : According to a third embodiment, the composite fibers according to the invention can be produced according to a process comprising the successive steps consisting of:
a) la dispersion de graphène dans un solvant, en présence d'un agent stabilisant lié de façon covalente ou non covalente au graphène et d'un liant polymère, pour former une composition d' enduction,  a) dispersing graphene in a solvent, in the presence of a stabilizing agent covalently or non-covalently bound to graphene and a polymeric binder, to form a coating composition,
b) l' enduction d'une fibre naturelle ou synthétique par ladite composition d'enduction,  b) coating a natural or synthetic fiber with said coating composition,
c) le passage de la fibre composite obtenue dans une solution de coagulation, comprenant au moins un agent de coagulation,  c) passing the composite fiber obtained in a coagulation solution, comprising at least one coagulation agent,
d) l'extraction, le lavage éventuel et le séchage de la fibre composite coagulée.  d) extraction, possible washing and drying of the coagulated composite fiber.
On obtient ainsi une fibre multicouche renfermant : - un coeur formé d'une fibre naturelle ou synthétique, A multilayer fiber is thus obtained containing: a core formed of a natural or synthetic fiber,
- une écorce renfermant un liant polymère et du graphène . Les solvants, agents stabilisants, liants polymères et solutions de coagulation utilisés dans ce procédé peuvent être choisis parmi ceux mentionnés précédemment. Un exemple d'un tel procédé a été décrit dans la demande FR 2 946 178, à laquelle on pourra se référer pour plus de détails. a bark containing a polymeric binder and graphene. The solvents, stabilizing agents, polymeric binders and coagulation solutions used in this process may be chosen from those mentioned above. An example of such a process has been described in the application FR 2 946 178, to which reference may be made for further details.
Il est bien entendu que les procédés décrits ci- dessus peuvent éventuellement comprendre d'autres étapes préliminaires, intermédiaires et/ou subséquentes à celles mentionnées précédemment, pour autant que celles-ci n'affectent pas négativement la formation des fibres composites recherchées. It is understood that the methods described above may optionally comprise other preliminary stages, intermediate and / or subsequent to those mentioned above, provided that these do not adversely affect the formation of the desired composite fibers.
Ainsi, ils peuvent notamment comprendre une étape de bobinage, et éventuellement une étape d'étirage à chaud réalisée entre l'étape de séchage et l'étape de bobinage. Ils peuvent aussi inclure à différents moments des étirements dans des solvants. Thus, they may include a winding step, and possibly a hot stretching step performed between the drying step and the winding step. They may also include stretches in solvents at different times.
En outre, bien que les fibres composites obtenues selon ce procédé soient intrinsèquement conductrices, leur conductivité électrique peut encore être améliorée par des traitements thermiques. In addition, although the composite fibers obtained by this method are intrinsically conductive, their electrical conductivity can be further improved by heat treatments.
Quel que soit le mode de réalisation mis en œuvre pour les préparer, les fibres composites selon l'invention peuvent comprendre d'autres charges conductrices carbonées en plus du graphène, en particulier une ou plusieurs charges choisies parmi les nanotubes de carbone, les nanofibres de carbone, et leurs mélanges . Les nanofibres de carbone sont, comme les nanotubes de carbone, des nanofilaments généralement produits par dépôt chimique en phase vapeur (ou CVD) à partir d'une source carbonée qui est décomposée sur un catalyseur comportant un métal de transition (Fe, Ni, Co, Cu) , en présence d'hydrogène, à des températures de 500 à 1200°C. Toutefois, ces deux charges carbonées se différencient par leur structure (I. MARTIN-GULLON et al., Carbon, Vol. 44, 1572-1580, 2006) . En effet, les nanotubes de carbone sont constitués d'un ou plusieurs feuillets de graphène enroulés de manière concentrique pour former un cylindre ayant un diamètre de 1 à 100 nm. Au contraire, les nanofibres de carbone se composent de zones graphitiques plus ou moins organisées (ou empilements turbostratiques ) dont les plans sont inclinés à des angles variables par rapport à l'axe de la fibre. Ces empilements peuvent prendre la forme de plaquettes, d'arêtes de poisson ou de coupelles empilées pour former des structures ayant un diamètre allant généralement de 100 nm à 500 nm voire plus . Whatever the embodiment used to prepare them, the composite fibers according to the invention may comprise other conductive carbonaceous fillers in addition to graphene, in particular one or more fillers chosen from carbon nanotubes, nanofibres of carbon, and mixtures thereof. Carbon nanofibers are, like carbon nanotubes, nanofilaments generally produced by chemical vapor deposition (or CVD) from a carbon source that is decomposed on a catalyst having a transition metal (Fe, Ni, Co, Cu) in the presence of hydrogen at temperatures of 500 to 1200 ° C. However, these two carbonaceous charges are differentiated by their structure (I. MARTIN-GULLON et al., Carbon, Vol 44, 1572-1580, 2006). Indeed, the carbon nanotubes consist of one or more sheets of graphene wound concentrically to form a cylinder having a diameter of 1 to 100 nm. On the contrary, carbon nanofibers are composed of more or less organized graphitic zones (or turbostratic stacks) whose planes are inclined at variable angles with respect to the axis of the fiber. These stacks can take the form of platelets, fish bones or stacked cups to form structures generally ranging in diameter from 100 nm to 500 nm or more.
Les nanotubes de carbone utilisables dans la présente invention sont avantageusement de type multi- parois, renfermant de 5 à 15 parois, et sont de préférence obtenus suivant un procédé de dépôt chimique en phase vapeur (CVD) . Ils ont avantageusement un diamètre moyen allant de 0,1 à 100 nm et une longueur de 0,1 à 20 pm. Des exemples de nanotubes de carbone bruts sont ceux disponibles dans le commerce auprès de la société ARKEMA sous la dénomination commerciale Graphistrength C100. The carbon nanotubes that can be used in the present invention are advantageously of multi-wall type, containing from 5 to 15 walls, and are preferably obtained by a chemical vapor deposition (CVD) process. They advantageously have a mean diameter ranging from 0.1 to 100 nm and a length of 0.1 to 20 μm. Examples of crude carbon nanotubes are those commercially available from ARKEMA under the trademark Graphistrength C100.
Des exemples de nanofibres de carbone sont celles disponibles sous la dénomination commerciale VGCF auprès de la société SHOWA DENKO . Plus particulièrement, les fibres selon l'invention peuvent comprendre un assemblage de nanotubes de carbone et de graphène susceptible d'être obtenu par décomposition à une température de 500 à 1500°C d'une source de carbone à l'état gazeux, mise en contact avec un catalyseur A actif pour la synthèse de nanotubes de carbone et d'un catalyseur B actif pour la synthèse de graphène. Cet assemblage peut ainsi être obtenu en adaptant le procédé de synthèse de graphène décrit précédemment pour y ajouter le catalyseur A. Ce dernier peut notamment comprendre un métal tel que le fer, le cobalt, le nickel, le molybdène, le titane et leurs mélanges, supporté sur un support inerte solide, par exemple de l'alumine. Un tel catalyseur peut notamment être préparé par imprégnation d'un substrat sec à l'aide d'une solution d'imprégnation aqueuse ou alcoolique comprenant des sels métalliques. Examples of carbon nanofibers are those available under the trade name VGCF from SHOWA DENKO. More particularly, the fibers according to the invention may comprise an assembly of carbon and graphene nanotubes capable of being obtained by decomposition at a temperature of 500 to 1500 ° C. of a source of carbon in the gaseous state, implemented contact with an active catalyst A for the synthesis of carbon nanotubes and an active catalyst B for the synthesis of graphene. This assembly can thus be obtained by adapting the graphene synthesis process described above to add catalyst A. The latter may in particular comprise a metal such as iron, cobalt, nickel, molybdenum, titanium and mixtures thereof. supported on a solid inert support, for example alumina. Such a catalyst may especially be prepared by impregnating a dry substrate with an aqueous or alcoholic impregnation solution comprising metal salts.
Par ailleurs, les fibres composites selon l'invention peuvent renfermer au moins un polymère conducteur. Par « polymère conducteur », on entend un homo- ou copolymère dont la chaîne principale renferme des doubles liaisons conjuguées - par exemple sous forme d'un ou plusieurs (hétéro ) cycles aromatiques - et qui forme, après oxydation éventuelle et dopage à l'aide d'au moins un agent dopant, un sel ou complexe présentant des propriétés de conduction électrique. Des exemples de polymères conducteurs utilisables sont notamment les homo- et copolymères comprenant un ou plusieurs monomères choisis parmi l'aniline, le pyrrole, le thiophène éventuellement substitué, l'acétylène, le phénylène vinylène, le sulfure de phénylène et leurs mélanges. Un exemple de polymère de thiophène substitué est le poly (3, 4-éthylènedioxythiophène) ou PEDOT . Le PEDOT et la polyaniline (PANI) sont préférés pour une utilisation dans la présente invention. La polyaniline existe sous différents états d'oxydation, liés aux proportions de fonctions imine et aminé contenues dans la molécule. On préfère selon l'invention utiliser 1 'éméraldine, qui correspond à l'état d'oxydation intermédiaire de la polyaniline, présentant les meilleures propriétés électriques . Moreover, the composite fibers according to the invention may contain at least one conductive polymer. By "conducting polymer" is meant a homo- or copolymer whose main chain contains conjugated double bonds - for example in the form of one or more (hetero) aromatic rings - and which forms, after possible oxidation and doping with the using at least one doping agent, a salt or complex having electrical conduction properties. Examples of usable conductive polymers include homo- and copolymers comprising one or more monomers selected from aniline, pyrrole, optionally substituted thiophene, acetylene, phenylene vinylene, phenylene sulfide and mixtures thereof. An example of a substituted thiophene polymer is the poly (3,4-ethylenedioxythiophene) or PEDOT. PEDOT and polyaniline (PANI) are preferred for use in the present invention. Polyaniline exists under different oxidation states, related to the proportions of imine and amine functions contained in the molecule. It is preferred according to the invention to use emeraldine, which corresponds to the intermediate oxidation state of polyaniline, having the best electrical properties.
Des exemples d'agents dopants comprennent les acides protoniques forts, ayant un pKa inférieur à 3, tels que l'acide chlorhydrique, l'acide sulfurique et ses sels tels que le dodécyl sulfate de sodium, les acides phosphoniques et les composés sulfoniques, notamment l'acide 2-acrylamido 2-méthylpropane sulfonique (AMPS), l'acide dodécylbenzène sulfonique, l'acide camphosulfonique, l'acide toluène sulfonique, l'acide méthane sulfonique et les polymères à fonction (s) suifonique ( s ) , tels que le poly(acide styrène sulfonique) qui est l'agent dopant préfèrentiellement utilisé en association avec le PEDOT pour former une solution colloïdale PEDOT :PSS. D'autres agents dopants comprennent le polyacrylamide et le poly (acide acrylique) . Les sels ou complexes de polymères conducteurs et d'agents dopants peuvent être obtenus par voie chimique ou électrochimique, suivant des techniques connues de l'homme du métier. Certains sont par ailleurs disponibles dans le commerce, notamment auprès de la société PANIPOL. Examples of doping agents include strong protonic acids having a pKa of less than 3, such as hydrochloric acid, sulfuric acid and its salts such as sodium dodecyl sulphate, phosphonic acids and sulphonic compounds, especially 2-acrylamido-2-methylpropanesulphonic acid (AMPS), dodecylbenzenesulfonic acid, camphorsulfonic acid, toluenesulphonic acid, methanesulphonic acid and sulphonic function (s) polymers, such as that the poly (styrene sulfonic acid) which is the doping agent preferably used in combination with the PEDOT to form a colloidal solution PEDOT: PSS. Other doping agents include polyacrylamide and polyacrylic acid. The salts or complexes of conductive polymers and doping agents can be obtained chemically or electrochemically, according to techniques known to those skilled in the art. Some are also available commercially, especially from PANIPOL.
Ces polymères conducteurs peuvent être incorporés dans les fibres composites selon l'invention dans l'une ou l'autre des variantes décrites précédemment, en les mélangeant au liant polymère avant l'étape de coagulation . These conductive polymers can be incorporated in the composite fibers according to the invention in one of or the other of the variants described above, by mixing them with the polymeric binder before the coagulation step.
La présente invention a également pour objet l'utilisation des fibres composites conductrices précitées pour la fabrication de nez, d'ailes ou de carlingues de fusées ou d'avions ; d'armures de flexible off-shore ; d'éléments de carrosserie automobile, de châssis moteur ou de pièces support pour l'automobile ; de revêtements de sièges automobiles ; d'éléments de charpentes dans le domaine du bâtiment ou des ponts et chaussées ; d'emballages et de textiles antistatiques, notamment de rideaux antistatiques, de vêtements antistatiques (par exemple, de sécurité ou pour salle blanche) ou de matériaux pour la protection de silos ou le conditionnement et/ou le transport de poudres ou de matériaux granulaires ; d'éléments d'ameublement, notamment de mobilier pour salle blanche ; de filtres ; de dispositifs de blindage électromagnétique, notamment pour la protection de composants électroniques ; de câbles conducteurs ; de capteurs, notamment de capteurs de déformation ou de contraintes mécaniques ; d'électrodes ; de dispositifs de stockage d'hydrogène ; de dispositifs biomédicaux tels que des fils de suture, des prothèses ou des cathéters ; d'afficheurs, de claviers ou de connecteurs intégrés à des vêtements ; ou de récepteurs et émetteurs d'ondes électromagnétiques. The present invention also relates to the use of the above-mentioned conductive composite fibers for the manufacture of nose, wings or cockles of rockets or airplanes; off-shore flexible armor; automotive bodywork components, engine chassis or automobile support parts; automotive seat coverings; structural elements in the field of buildings or bridges and roadways; packaging and antistatic textiles, in particular antistatic curtains, antistatic clothing (for example, safety or clean room) or materials for the protection of silos or the packaging and / or transport of powders or granular materials; furnishing items, including clean room furniture; filters; electromagnetic shielding devices, in particular for the protection of electronic components; conductive cables; sensors, in particular deformation sensors or mechanical stresses; electrodes; hydrogen storage devices; biomedical devices such as sutures, prostheses or catheters; displays, keyboards or connectors incorporated into clothing; or receivers and emitters of electromagnetic waves.
La fabrication de ces pièces composites peut être réalisée suivant différents procédés, impliquant en général une étape d'imprégnation des fibres composites conductrices selon l'invention par une composition polymérique renfermant au moins un matériau thermoplastique, élastomère ou thermodurcissable . Cette étape d'imprégnation peut elle-même être effectuée suivant différentes techniques, en fonction notamment de la forme physique de la composition polymérique utiliséeThe manufacture of these composite parts can be carried out according to various processes, generally involving a step of impregnating the conductive composite fibers according to the invention with a composition polymeric material comprising at least one thermoplastic, elastomeric or thermosetting material. This impregnation step may itself be carried out according to various techniques, depending in particular on the physical form of the polymeric composition used.
(pulvérulente ou plus ou moins liquide) . L'imprégnation des fibres composites conductrices est de préférence réalisée suivant un procédé d'imprégnation en lit fluidisé, dans lequel la composition polymérique se trouve à l'état de poudre. Des fibres pré-imprégnées sont ainsi obtenues. (pulverulent or more or less liquid). The impregnation of the conductive composite fibers is preferably carried out according to a fluidized bed impregnation process, in which the polymeric composition is in the form of powder. Pre-impregnated fibers are thus obtained.
On obtient des semi-produits qui sont ensuite utilisés dans la fabrication de la pièce composite recherchée. Différents tissus de fibres pré-imprégnées, de composition identique ou différente, peuvent être empilés pour former une plaque ou un matériau stratifié, ou en variante soumis à un procédé de thermoformage. En variante, les fibres pré-imprégnées peuvent être associées pour former des rubans qui sont susceptibles d'être utilisés dans un procédé d'enroulement filamentaire permettant l'obtention de pièces creuses de forme quasi-illimitée, par enroulement des rubans sur un mandrin ayant la forme de la pièce à fabriquer. Dans tous les cas, la fabrication de la pièce finie comprend une étape de consolidation de la composition polymérique, qui est par exemple fondue localement pour créer des zones de fixation des fibres pré-imprégnées entre elles et/ou solidariser les rubans de fibres pré-imprégnées dans le procédé d'enroulement filamentaire. variante encore, il est possible de préparer un à partir de la composition polymérique d'imprégnation, notamment au moyen d'un procédé d'extrusion ou de calandrage, ledit film ayant par exemple une épaisseur d'environ 100 pm, puis de le placer entre deux mats de fibres composites conductrices selon l'invention, l'ensemble étant alors pressé à chaud pour permettre l'imprégnation des fibres et la fabrication de la pièce composite. Semi-finished products are obtained which are then used in the manufacture of the desired composite part. Different preimpregnated fiber fabrics, of identical or different composition, can be stacked to form a plate or a laminated material, or alternatively subjected to a thermoforming process. As a variant, the pre-impregnated fibers may be combined to form ribbons which may be used in a filament winding process which makes it possible to obtain hollow pieces of almost unlimited shape, by winding the ribbons on a mandrel having the shape of the part to be made. In all cases, the manufacture of the finished part comprises a step of consolidating the polymeric composition, which is for example melted locally to create zones for fixing the fibers pre-impregnated with each other and / or to secure the fiber ribbons pre-impregnated with each other. impregnated in the filament winding process. alternatively, it is possible to prepare one from the polymeric composition impregnation, in particular by means of an extrusion or calendering process, said film having for example a thickness of about 100 μm, and then of placing it between two mats of conductive composite fibers according to the invention, the whole being then pressed hot to allow the impregnation of the fibers and the manufacture of the composite part.
Dans ces procédés, les fibres composites conductrices selon l'invention peuvent être tissées ou tricotées, seules ou avec d'autres fibres, ou être utilisées, seules ou en association avec d'autres fibres, pour la fabrication de câbles, de feutres ou de matériaux non-tissés. Des exemples de matériaux constitutifs de ces autres fibres comprennent, sans limitation : In these processes, the conductive composite fibers according to the invention can be woven or knitted, alone or with other fibers, or used, alone or in combination with other fibers, for the manufacture of cables, felts or nonwoven materials. Examples of materials constituting these other fibers include, without limitation:
- les fibres de polymère étiré, à base notamment : de polyamide tel que le polyamide 6 (PA-6), le polyamide 11 (PA-11), le polyamide 12 (PA-12), le polyamide 6.6 (PA-6.6), le polyamide 4.6 (PA-4.6), le polyamide 6.10 (PA-6.10) ou le polyamide 6.12 (PA-6.12), de copolymère bloc polyamide/polyéther (Pebax®) , de polyéthylène haute densité, de polypropylène ou de polyester tel que les polyhydroxyalcanoates et les polyesters commercialisés par DU PONT sous la dénomination commerciale Hytrel® ; stretched polymer fibers, based in particular on: polyamide such as polyamide 6 (PA-6), polyamide 11 (PA-11), polyamide 12 (PA-12), polyamide 6.6 (PA-6.6) the polyamide 4.6 (PA-4,6), polyamide-6,10 (PA-6.10) or polyamide 6.12 (PA-6.12), copolymer polyamide / polyether block (Pebax ®), high density polyethylene, polypropylene or polyester such as polyhydroxyalkanoates and polyesters marketed by Du Pont under the trade name Hytrel ®;
- les fibres de carbone ;  - carbon fibers;
- les fibres de verre, notamment de type E, R ou glass fibers, especially of type E, R or
S2 ; S2;
- les fibres d'aramide (Kevlar®) ; - aramid fibers (Kevlar ® );
- les fibres de bore ;  - boron fibers;
- les fibres de silice ;  - silica fibers;
- les fibres naturelles telles que le lin, le chanvre, le sisal le coton ou la laine ; et - leurs mélanges, tels que les mélanges de fibres de verre, carbone et aramide. - natural fibers such as linen, hemp, sisal cotton or wool; and - their mixtures, such as fiberglass, carbon and aramid blends.
L'invention sera mieux comprise à la lumière des exemples ci-dessous qui sont donnés à des fins d'illustration uniquement et n'ont pas pour but de limiter la portée de l'invention. The invention will be better understood in light of the examples below which are given for purposes of illustration only and are not intended to limit the scope of the invention.
EXEMPLES EXAMPLES
Exemple 1 : Fabrication de fibres composites selon 1' invention Example 1 Manufacture of Composite Fibers According to the Invention
Etape 1 : synthèse d'assemblages de nanotubes de carbone et de graphène (NTC/GP) Step 1: Synthesis of assemblages of carbon nanotubes and graphene (NTC / GP)
1-1. Préparation du catalyseur A 1-1. Preparation of Catalyst A
Dans un bêcher de 250 ml, on a préparé 37,5 ml d'une solution aqueuse d'acide citrique à une concentration de 0,4 M, à laquelle on a ajouté 1,1 g de nitrate de cobalt In a 250 ml beaker, 37.5 ml of an aqueous solution of citric acid at a concentration of 0.4 M was prepared, to which 1.1 g of cobalt nitrate was added.
(Co(N03)2), 6H20) et 3,1 g de nitrate de fer (Fe(N03)3), 9H2O) . On a ajusté le pH de la solution obtenue à une valeur de 6 par addition, goutte-à-goutte et sous agitation, d'ammoniaque (NH4OH) . Le rapport molaire entre le nitrate de fer et le nitrate de cobalt dans la solution aqueuse était sensiblement de l'ordre de 2. On a placé cette solution aqueuse dans un cristallisoir en Pyrex à une température de 80 °C pendant une durée sensiblement de l'ordre de 12 h de façon à former un gel homogène sensiblement déshydraté. (Co (NO 3 ) 2 ), 6H 2 O) and 3.1 g of iron nitrate (Fe (NO 3 ) 3 ), 9H 2 O). The pH of the resulting solution was adjusted to a value of 6 by adding, dropwise and stirring, ammonia (NH 4 OH). The molar ratio of iron nitrate to cobalt nitrate in the aqueous solution was substantially of the order of 2. This aqueous solution was placed in a Pyrex crystallizer at a temperature of 80 ° C. for a period of substantially one hour. order of 12 hours to form a substantially dehydrated homogeneous gel.
On a chauffé le gel homogène ainsi obtenu à une température de l'ordre de 200°C de façon à décomposer l'acide citrique. On a observé alors l'expansion du gel homogène en une mousse que l'on a laissé se développer pendant environ 30 min jusqu'à stabilisation. On a broyé ensuite délicatement cette mousse de façon à former une poudre que l'on a chauffée à une température de 400°C pendant 4 heures à l'air atmosphérique. On a obtenu ainsi une poudre cristalline de ferrite de cobalt. The homogeneous gel thus obtained was heated to a temperature of the order of 200 ° C. so as to decompose citric acid. The expansion of the homogeneous gel was then observed to foam which was allowed to develop for about 30 minutes until stabilization. This foam was then crushed gently to form a powder which was heated at 400 ° C for 4 hours in atmospheric air. A crystalline powder of cobalt ferrite was thus obtained.
Cette poudre présentait une unique phase d'oxyde possédant une structure de type spinelle avec une taille de domaine cristallin comprise entre 14 nm et 20 nm (déterminée par diffraction des rayons X) et une surface spécifique de 7 m2/g. This powder had a single oxide phase having a spinel type structure with a crystalline domain size of between 14 nm and 20 nm (determined by X-ray diffraction) and a specific surface area of 7 m 2 / g.
1-2. Préparation du catalyseur B 1-2. Catalyst B preparation
On a préparé un catalyseur à partir d'alumine Puralox® SCCa-5/150 de diamètre médian égal à environ 85 μιη et de surface spécifique 160 m2/g. Dans un réacteur de 1 1 muni d'une double enveloppe chauffé à 120°C, on a introduit 100 g d'alumine et on a balayé à l'air. Au moyen d'une pompe, on a injecté alors en continu 80 ml d'une solution à 45 g/1 de molybdate d'ammonium tétrahydraté, puis 560 ml d'une solution à 675 g/1 de nitrate de fer nonahydraté. Le ratio visé (masse de métal/masse de catalyseur) étant de 32% pour le fer et 3% pour le molybdène, la durée d'addition a été de 25 h. Le catalyseur a ensuite été chauffé in-situ à 220 °C sous balayage d'air sec pendant 8 heures, puis placé dans un four à moufle à 400°C pendant 8 heures. A catalyst was prepared from Puralox ® SCCa-5/150 alumina with a median diameter of approximately 85 μιη and a specific surface area of 160 m 2 / g. In a 1 1 reactor equipped with a double jacket heated to 120 ° C, 100 g of alumina was introduced and flushed with air. 80 ml of a 45 g / l solution of ammonium molybdate tetrahydrate were then continuously injected, followed by 560 ml of a 675 g / l solution of iron nitrate nonahydrate. The target ratio (metal mass / catalyst mass) being 32% for iron and 3% for molybdenum, the duration of addition was 25 h. The catalyst was then heated in situ at 220 ° C under dry air for 8 hours and then placed in a muffle furnace at 400 ° C for 8 hours.
1-3. Synthèse de l'assemblage NTC/GP 1-3. Synthesis of the NTC / GP assembly
On a effectué un test catalytique en mettant une masse d'environ 1,9 g du catalyseur A et d'environ 0,6 g du catalyseur B dans un réacteur en quartz de 5 cm de diamètre et de 1 mètre de hauteur de chauffe efficace. A catalytic test was carried out by putting a mass of about 1.9 g of catalyst A and about 0.6 g catalyst B in a quartz reactor of 5 cm in diameter and 1 meter effective heating height.
On a chauffé à 650 °C sous 2,66 1/mn d'azote pendant 30 minutes puis on a maintenu un palier de réduction pendant 30 minutes sous 2 1/mn d'azote et 0,66 1/mn d'hydrogène. Une fois ce palier atteint, on a introduit un débit d'éthylène de 2 1/mn et d'hydrogène de 0,66 1/mn. Après 60 minutes, on a arrêté le chauffage et on a refroidi le réacteur sous un courant d'azote de 2 1/mn.It was heated at 650 ° C. under 2.66 l / min of nitrogen for 30 minutes and then a reduction stage was maintained for 30 minutes under 2 l / min of nitrogen and 0.66 l / min of hydrogen. Once this plateau reached, an ethylene flow rate of 2 l / min and hydrogen of 0.66 l / min was introduced. After 60 minutes, the heating was stopped and the reactor was cooled under a stream of nitrogen of 2 l / min.
La quantité de produit récupéré en fin de réaction a été de 47 g. Le ratio massique NTC/GP théorique dans cet essai était de 90/10. The amount of product recovered at the end of the reaction was 47 g. The theoretical NTC / GP mass ratio in this test was 90/10.
On a préparé de manière similaire un assemblage de nanotubes de carbone et de graphène (NTC/GP) dans un rapport en poids de 80/20.  Similarly, an assembly of carbon and graphene nanotubes (CNT / GP) in a weight ratio of 80/20 was prepared.
Etape 2 : Réalisation des fibres composites Trois dispersions aqueuses ont été réalisées, respectivement à partir des deux assemblages précités et de NTC sans graphène. Pour ce faire, on a introduit dans de l'eau 0,9% en poids des charges précitées et 1,2% en poids d'un tensioactif (Brij® 78) . Ces suspensions ont ensuite été passées à la microsonde à ultrasons pendantStep 2: Production of Composite Fibers Three aqueous dispersions were carried out, respectively from the two aforementioned assemblies and from NTC without graphene. To this was charged in water 0.9% by weight of the aforementioned charges and 1.2% by weight of a surfactant (Brij ® 78). These suspensions were then passed to the ultrasound microprobe for
60 minutes. Une solution aqueuse de poly (alcool vinylique) a ensuite été ajoutée à chacune pour obtenir une solution de filage. Celle-ci a alors été injectée dans un bain de coagulation composé de sulfate de sodium concentré à 320 g/1 dans de l'eau et chauffé à 40°C. La fibre a ensuite été lavée dans un premier bain contenant 0,1% de tétraborate de sodium dans l'eau, puis on l'a fait passer dans un second bain contenant uniquement de l'eau. La fibre a ensuite été séchée et bobinée. On a obtenu une fibre mono-filament. Les fibres obtenues à partir d'un ratio NTC/GP de 90/10 et de 80/20 avaient respectivement une teneur théorique en graphène de 1,1 et 2,3% en poids. Leur diamètre moyen était d'environ 45 pm. 60 minutes. An aqueous solution of polyvinyl alcohol was then added to each to obtain a spinning solution. This was then injected into a coagulation bath composed of sodium sulfate, concentrated to 320 g / l in water and heated to 40 ° C. The fiber was then washed in a first bath containing 0.1% sodium tetraborate in water and then passed to a second bath containing only the water. The fiber was then dried and coiled. Monofilament fiber was obtained. The fibers obtained from a NTC / GP ratio of 90/10 and 80/20 respectively had a theoretical graphene content of 1.1 and 2.3% by weight. Their average diameter was about 45 μm.
Exemple 2 : Essais mécaniques et de conductivité électrique Example 2: Mechanical Tests and Electrical Conductivity
Des essais de traction mécanique ont été réalisés sur les trois fibres obtenues à l'Exemple 1. Les résultats obtenus, moyennés sur 5 éprouvettes, sont rassemblés dans le Tableau 1 ci-dessous. Mechanical tensile tests were carried out on the three fibers obtained in Example 1. The results obtained, averaged over 5 test pieces, are collated in Table 1 below.
Tableau 1 Table 1
Figure imgf000026_0001
Figure imgf000026_0001
Il ressort de cet essai que la contrainte à la rupture des fibres contenant du graphène est supérieure à celle des fibres qui en sont dépourvues. It is apparent from this test that the breaking stress of graphene-containing fibers is greater than that of fibers which lack them.
On a par ailleurs mesuré la conductivité électrique des fibres de l'Exemple 1. Les résultats obtenus, moyennés sur 6 éprouvettes, sont présentés dans le tableau 2 ci-dessous. Tableau 2 The electrical conductivity of the fibers of Example 1 was also measured. The results obtained, averaged over 6 test pieces, are shown in Table 2 below. Table 2
Figure imgf000027_0001
Figure imgf000027_0001
Les fibres ne renfermant pas de graphène présentent une résistance électrique supérieure au seuil de détection de l'appareil utilisé (multimètre Keithley® 2000), due à l'orientation des NTC le long de la fibre, qui est défavorable à la transmission du courant. Au contraire, les fibres contenant du graphène ont une conductivité électrique satisfaisante, qui pourrait être encore améliorée par un traitement thermique. Fibers that do not contain graphene have an electrical resistance greater than the detection threshold of the device used (Keithley ® 2000 multimeter), due to the orientation of the NTC along the fiber, which is unfavorable to the transmission of the current. In contrast, graphene-containing fibers have satisfactory electrical conductivity, which could be further enhanced by heat treatment.

Claims

REVENDICATIONS
1. Fibres composites conductrices, renfermant du graphène dispersé dans une matrice polymérique, caractérisées en ce que le graphène se présente sous forme de particules d'une épaisseur de moins de 100 nm, de préférence de moins de 50 nm, plus préfèrentiellement de moins de 15 nm, et de dimensions latérales d'environ 1 pm, préfèrentiellement de 50 à 800, plus préfèrentiellement encore de 100 à 600 nm, voire de 100 à1. Conductive composite fibers containing graphene dispersed in a polymer matrix, characterized in that the graphene is in the form of particles having a thickness of less than 100 nm, preferably less than 50 nm, more preferably less than 15 nm, and of lateral dimensions of about 1 μm, preferably from 50 to 800, more preferably from 100 to 600 nm, or even 100 to
500 nm. 500 nm.
2. Fibres composites selon la revendication 1, caractérisées en ce que le graphène est obtenu par un procédé de dépôt chimique en phase vapeur (CVD) . 2. Composite fibers according to claim 1, characterized in that graphene is obtained by a chemical vapor deposition (CVD) process.
3. Fibres composites selon l'une des revendications 1 et 2, caractérisées en ce qu'elles renferment en outre une ou plusieurs charges choisies parmi les nanotubes de carbone, les nanofibres de carbone, et leurs mélanges. 3. Composite fibers according to one of claims 1 and 2, characterized in that they further contain one or more fillers selected from carbon nanotubes, carbon nanofibers, and mixtures thereof.
4. Fibres composites selon la revendication 3, caractérisées en ce qu'elles renferment un assemblage de nanotubes de carbone et de graphène susceptible d'être obtenu par décomposition à une température de 500 à4. Composite fibers according to claim 3, characterized in that they contain an assembly of carbon nanotubes and graphene obtainable by decomposition at a temperature of 500 to
1500°C d'une source de carbone à l'état gazeux, mise en contact avec un catalyseur A actif pour la synthèse de nanotubes de carbone et d'un catalyseur B actif pour la synthèse de graphène. 1500 ° C of a source of carbon in the gaseous state, brought into contact with an active catalyst A for the synthesis of carbon nanotubes and an active catalyst B for the synthesis of graphene.
5. Fibres composites selon l'une quelconque des revendications 1 à 4, caractérisées en ce qu'elles renferment en outre au moins un polymère conducteur, tel que le poly ( 3 , 4-éthylènedioxythiophène ) (PEDOT) et la polyaniline . 5. Composite fibers according to any one of claims 1 to 4, characterized in that they contain in addition at least one conductive polymer, such as that poly (3,4-ethylenedioxythiophene) (PEDOT) and polyaniline.
6. Fibres composites selon l'une quelconque des revendications 1 à 5, caractérisées en ce qu'elles renferment de 0,5 à 50% en poids, de préférence de 1 à 30% en poids, plus préfèrentiellement de 3,5 à 15% en poids de graphène. 6. Composite fibers according to any one of claims 1 to 5, characterized in that they contain from 0.5 to 50% by weight, preferably from 1 to 30% by weight, more preferably from 3.5 to 15% by weight. % by weight of graphene.
7. Procédé de fabrication des fibres composites selon l'une quelconque des revendications 1 à 6, caractérisé en ce qu'il consiste en un procédé de coagulation comprenant : 7. A method of manufacturing composite fibers according to any one of claims 1 to 6, characterized in that it consists of a coagulation process comprising:
- soit la coagulation sous forme de fibre, ou autour d'une fibre pré-formée, d'un mélange de graphène et de liant polymère, en le faisant passer dans une solution de coagulation,  either coagulation in the form of fiber, or around a pre-formed fiber, a mixture of graphene and a polymeric binder, by passing it through a coagulation solution,
- soit l'injection du graphène dispersé dans un solvant dans un co-écoulement d'une solution de coagulation renfermant un liant polymère.  or the injection of graphene dispersed in a solvent in a co-flow of a coagulation solution containing a polymeric binder.
8. Procédé selon la revendication 7, caractérisé en ce qu'il comprend les étapes successives consistant en : a) la formation d'une dispersion de graphène dans une solution de liant polymère, en présence d'au moins un agent stabilisant lié de façon covalente ou non covalente au graphène, 8. Method according to claim 7, characterized in that it comprises the successive steps consisting of: a) forming a graphene dispersion in a polymer binder solution, in the presence of at least one stabilizing agent bound in a covalent or non-covalent to graphene,
b) l'injection de ladite dispersion dans une solution de coagulation,  b) injecting said dispersion into a coagulation solution,
c) l'extraction de la fibre obtenue,  c) extracting the obtained fiber,
d) le lavage éventuel de ladite fibre,  d) the possible washing of said fiber,
e) le séchage de ladite fibre. e) drying said fiber.
9. Procédé selon la revendication 7, caractérisé en ce qu'il comprend les étapes successives consistant en : la dispersion de graphène dans un solvant à l'aide éventuellement d'un agent tensioactif, 9. Method according to claim 7, characterized in that it comprises the successive steps consisting in: the dispersion of graphene in a solvent possibly using a surfactant,
l'injection de la dispersion de graphène dans un co- écoulement d'une solution de coagulation renfermant un liant polymère,  injecting the graphene dispersion into a co-flow of a coagulation solution containing a polymeric binder,
l'extraction de la fibre obtenue,  extraction of the obtained fiber,
le lavage éventuel de ladite fibre, et  the eventual washing of said fiber, and
le séchage de ladite fibre.  drying said fiber.
10. Procédé selon la revendication 7, caractérisé en ce qu'il comprend les étapes successives consistant en : a) la dispersion de graphène dans un solvant, en présence d'un agent stabilisant lié de façon covalente ou non covalente au graphène et d'un liant polymère, pour former une composition d' enduction, 10. Process according to claim 7, characterized in that it comprises the successive stages consisting of: a) the dispersion of graphene in a solvent, in the presence of a stabilizing agent covalently or non-covalently bound to graphene and of a polymeric binder, to form a coating composition,
b) l' enduction d'une fibre naturelle ou synthétique par ladite composition d'enduction,  b) coating a natural or synthetic fiber with said coating composition,
c) le passage de la fibre composite obtenue dans une solution de coagulation, comprenant au moins un agent de coagulation,  c) passing the composite fiber obtained in a coagulation solution, comprising at least one coagulation agent,
d) l'extraction, le lavage éventuel et le séchage de la fibre composite coagulée.  d) extraction, possible washing and drying of the coagulated composite fiber.
11. Utilisation des fibres composites conductrices selon l'une quelconque des revendications 1 à 6 pour la fabrication de nez, d'ailes ou de carlingues de fusées ou d'avions ; d'armures de flexible off-shore ; d'éléments de carrosserie automobile, de châssis moteur ou de pièces support pour l'automobile ; de revêtements de sièges automobiles ; d'éléments de charpentes dans le domaine du bâtiment ou des ponts et chaussées ; d'emballages et de textiles antistatiques, notamment de rideaux antistatiques, de vêtements antistatiques (par exemple, de sécurité ou pour salle blanche) ou de matériaux pour la protection de silos ou le conditionnement et/ou le transport de poudres ou de matériaux granulaires ; d'éléments d'ameublement, notamment de mobilier pour salle blanche ; de filtres ; de dispositifs de blindage électromagnétique, notamment pour la protection de composants électroniques ; de câbles conducteurs ; de capteurs, notamment de capteurs de déformation ou de contraintes mécaniques ; d'électrodes ; de dispositifs de stockage d'hydrogène ; de dispositifs biomédicaux tels que des fils de suture, des prothèses ou des cathéters ; d'afficheurs, de claviers ou de connecteurs intégrés à des vêtements ; ou de récepteurs et émetteurs d'ondes électromagnétiques . 11. Use of the conductive composite fibers according to any one of claims 1 to 6 for the manufacture of nose, wings or cabins of rockets or airplanes; off-shore flexible armor; automotive bodywork components, engine chassis or automobile support parts; automotive seat coverings; structural elements in the field of buildings or bridges and roadways; packaging and antistatic textiles, in particular antistatic curtains, antistatic clothing (for example, safety or clean room) or materials for the protection of silos or the packaging and / or transport of powders or granular materials; furnishing items, including clean room furniture; filters; electromagnetic shielding devices, in particular for the protection of electronic components; conductive cables; sensors, in particular deformation sensors or mechanical stresses; electrodes; hydrogen storage devices; biomedical devices such as sutures, prostheses or catheters; displays, keyboards or connectors incorporated into clothing; or receivers and emitters of electromagnetic waves.
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