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    • 专利摘要:
    Material comprising a porous composite material support comprising at least one binder-based polymeric phase based on at least one polymer chosen from thermoplastic polymers, elastomers and elastomer thermoplastics, and one or more fillers selected from thermal conductive fillers, pores of the support made of porous composite material being partially or completely filled with at least one phase-change material. Process for the manufacture of this material
    公开号:FR3034775A1
    申请号:FR1553213
    申请日:2015-04-13
    公开日:2016-10-14
    发明作者:Arnaud Prebe；Bruno Dufour；Fabrice Chopard；Nicolas Garois；Philippe Sonntag
    申请人:Hutchinson SA；
    IPC主号:
    专利说明:

    [0001] The invention relates to a new material for thermal storage having improved properties, this material comprising a support of porous thermally conductive material, the pores of which are filled with a phase-change material. (MCP). The invention also relates to a process for the manufacture of this material and its uses. STATE OF THE PRIOR ART Materials for thermal storage are used in different applications. They are found in areas such as the control of temperature by inertia in the building or in the exploitation of intermittent renewable energy sources. We can also consider exploiting the heat generated by electrical devices such as computers, servers, or batteries, provided that the material capable of storing energy is also electrical insulation. To produce a material for the storage of thermal energy, we find in the literature mainly three processes. The first method consists in encapsulating the MCP or adsorbing it on a support before its formulation in a composition of matter.
    [0002] For example, US20130298991 describes the use of inorganic fillers adsorbent MCP. The mixture is then formulated with a cement binder and an aqueous solvent to produce a cement containing MCP. The adsorption on the load is an additional step in the manufacture of cement. W003 / 099427, US5456852, US5916478 and WO2007 / 107171 disclose methods of encapsulating MCP to form particles having a PCM core and a polymeric coating. These particles are then dispersed in a support. In all cases, no thermal conductive load is incorporated in the support and the thermal conductivity of these materials is not evaluated. This method has the disadvantage of requiring complex steps of synthesis of polymeric shells. MCP-based materials encapsulated in polymeric matrices are not easily recyclable. A second method involves directly mixing the MCP with a binder, or mixing the MCP with a monomer which is then polymerized to form a binder in the presence of MCP. The binder ensures the cohesion of the material.
    [0003] For example W003085346 discloses a wall covering containing MCP particles that are adsorbed in a polymeric wall covering layer, or attached to an adsorbent layer of the wallcovering.
    [0004] EP693542 discloses a composition based on PCMs, water and water-swellable cross-linkable polymers. The mixture gives a composition in which MCP is dispersed in a hydrogel. WO2007 / 040395 describes the polymerization of monomers of which at least one is directly linked to a PCM.
    [0005] In all these materials, the MCP is associated with a non-conductive thermal support, thus the propagation of heat within the support of / to the MCP is very small. This design of the material causes a low reactivity of the system to changes in temperature. FR2993894 and US20050020768 describe materials obtained from a silicone-based matrix and PCM. In FR2993894 it is taught to incorporate thermally conductive fillers in the silicone matrix. However, since the amounts of thermally conductive fillers are small, the thermal conductivity values obtained are also low. The materials of the prior art being obtained from liquid precursors which are formulated and then crosslinked are not recyclable.
    [0006] Finally, the morphology of the materials of the prior art is different from that of the materials of the invention which have the particularity of being made of a porous support whose pores host the PCM. US20050020768 discloses a fine and split MCP dispersion in a crosslinked silicone matrix, while the method of the invention provides access to a material comprising a continuous phase of MCP if desired. WO200662610 discloses mixing MCP with elastomeric thermoplastic materials of the very low density polyethylene type, copolymer of ethylene and propylene as well as copolymers of styrene-butadiene-styrene and styrene-ethylene-butadiene-styrene. Non-heat conductive fillers such as silicates are used in the manufacture of the material to enhance the retention of MCP in the polymer. US5053446 discloses the production of a composite based on a polyolefin and a PCM and from 10 to 50% by mass of fillers such as silica or calcium and silicon metaphosphate which make it possible to improve the retention of the loads by the material. No thermally conductive filler is used, the thermal conductivity of the material is not mentioned. A third method comprises in a first step the manufacture of a porous structure in which, in a second step, the PCM is introduced. Thus US2002 / 0147242 describes the production of an open-pored polyurethane foam, the pores of which are filled with MCP. US2002 / 0147242 teaches that the porosity must be maximized in volume in order to allow filling with a high amount of MCP. US5637389 discloses the joint use of an encapsulated polymer foam and MCP in the manufacture of a thermally insulating material that can be used in shoe soles. No thermally conductive charge is used.
    [0007] It is known to incorporate thermal conductive fillers in a polymeric matrix. However, the incorporation of thermal conductive fillers in a large amount in a polymer matrix presents difficulties: The more charges are introduced into a polymer matrix, the higher the viscosity of the mixture and the more difficult it is to efficiently transform the mixture by the methods. 10 of usual plastics. This problem has been solved in various ways in the prior art: by the incorporation of charges in limited quantities in the final composite which also limits the thermal conductivity, by the use of low viscosity polymer precursors which are then crosslinked, or else by the use of a binder polymer in solution in a solvent which is then evaporated. The preparation of a thermally conductive solvent material presents problems of storage, handling and recycling of large quantities of solvents, which represent serious environmental and sanitary disadvantages in the case of organic solvents. The manufacture of a polymeric composite material by a solvent route can make it possible to obtain a porous material, but whose porosity is difficult to control and of a thickness necessarily reduced to films of a few hundred micrometers. A thermal conductive material prepared from liquid precursors that are subsequently crosslinked is not transformable or recyclable. On the other hand, the variety of polymeric bases which can be employed in these processes is limited and the process times are long. This type of process does not make it possible to obtain a porous material. Finally, such materials are not very conformable and therefore of limited interest in certain applications. Loads functionalized with groups that allow their incorporation in high quantities have the disadvantage of requiring a specific manufacturing step, which represents an additional cost for the material.
    [0008] The amounts of conductive fillers attainable in the melt with conventional polymers and ungrafted mineral or carbon fillers are, to date, less than 80% by volume. In addition, the melt processes of the prior art lead to a dense, non-porous composite. In applications where it is desired to rapidly capture the heat energy of a heat source, such as for example in electronic devices, it is necessary to have a material with a high thermal conductivity. Indeed, if the heat released is not picked up or propagated rapidly to a source of cold, there is a risk of heat accumulation that could lead to the decomposition of the connected parts of the heat source, with as a consequence, a start of fire. Similarly, in thermal energy storage applications, it is necessary to be able to transfer the heat energy to the MCP efficiently and quickly in order to increase the reactivity of the system in terms of storage and release of this energy. Depending on the application, the thermal conductive materials must also have a high conformability so as to match the shapes of the parts with which they are in contact. This property makes it possible to optimize heat fluxes. US20020141932 and WO200121551 disclose thermally conductive porous structures based on graphite and graphitized pitch. Thermal conductivities of at least 50W / m.K are described. The described material is obtained from pitch through pitch graphitization steps: high temperatures (> 1000 ° C) and non-oxidizing atmosphere. This porous material is then filled with MCP. Boron nitride is used in the manufacture of the material in US20020141932, but it is used in vaporization as a release agent for the graphitized material and not as a filler in the material. The graphitic nature of the materials taught by these documents makes them electrically conductive. These are non-deformable rigid materials in contrast to the polymeric support materials of the invention. Repeated phase changes during use are likely to cause volume expansions which themselves cause a risk of degradation and loss of cohesion in these prior art materials. Finally, the graphitic nature of these materials prevents their recycling. The object of the invention has been to provide a thermal conductive material capable of storing energy which overcomes the disadvantages of the prior art. In particular, an attempt has been made to develop a method which leads to a porous thermal conductive material whose porosity can be filled by MCP. It has also been sought to develop materials which are prepared by melting, which are optionally recyclable and which incorporate high amounts of thermal conductive fillers while having satisfactory cohesion. It has been sought to develop a process which can be carried out with mineral fillers or carbonaceous feeds without a step of functionalizing these feeds is necessary. It has also been sought to obtain a material that is conformable. SUMMARY OF THE INVENTION A first object of the invention is a material comprising: a support made of a porous composite material comprising at least (A) a binder-based polymeric phase based on at least one polymer chosen from thermoplastic polymers, elastomers and elastomer thermoplastics, and (B) one or more fillers chosen from heat-conducting fillers, the pores of the support made of porous composite material being filled partially or totally by: at least one material to be changed phase.
    [0009] The subject of the invention is also a process for the production of this material comprising: the manufacture of a porous composite material support comprising at least (A) a polymeric phase and (B) one or more fillers selected from among the fillers thermal conductive elements, - The partial or total filling of the porosity of the porous composite material support with at least one phase-change material. The invention further relates to a method for producing a porous carbonaceous conductive material, which process comprises: - producing a porous carbon support comprising at least (A) a polymeric phase and (B) one or more fillers chosen from thermal conductive fillers; Partial or total filling of the porosity of the porous carbon support with at least one phase change material, wherein the manufacture of the porous carbon carrier comprises the following steps: a) Hot melt mixing the polymeric phase (A), the charges (B), and a sacrificial polymeric phase (C), so as to obtain a mixture, b) shaping the mixture, c) removing the sacrificial polymeric phase, d) Pyrolysis or graphitization.
    [0010] The invention also relates to the use of the material defined above, or to the material obtained by one of the methods defined above, in one of the following applications: ICG70038 EN deposition 3034775 6 - heat sink in a electronic equipment, - energy storage medium. According to a preferred embodiment, the thermal conductive fillers (B) represent at least 60% by weight relative to the sum of the masses of the polymeric phase (A) and the charges (B). According to a preferred embodiment, the phase change material forms a continuous phase in the porosity of the porous composite material support.
    [0011] According to a preferred embodiment, the polymeric binder phase is based on at least one polymer chosen from: polyacrylonitrile, polyolefins, halogenated polymers, acrylic polymers, acrylates, methacrylates, vinyl acetates, polyethers, polyesters, polyamides, aromatic polymers, hydrogenated acrylonitrile-butadiene, copolymers of ethylene and an alkyl acrylate, polyisoprene, rubbers. According to a preferred embodiment, the fillers are chosen from: aluminum nitride, boron nitride, magnesium and silicon nitride, silicon carbide, diamond, graphite, graphene, nanotubes, carbon (CNT), carbon black, metal fillers such as aluminum, copper or silver, and mixtures thereof. According to a preferred embodiment, the porosity is at least 40% by volume relative to the total volume of the porous composite material support. According to a preferred embodiment, the phase-change material is chosen from hydrocarbon-based chains.
    [0012] According to a preferred embodiment, the manufacture of the porous composite material support comprises the following steps: a) Melt melt mixing of the polymeric phase (A), fillers (B), and a sacrificial polymeric phase (C), so as to obtain a mixture, b) shaping the mixture, c) removing the sacrificial polymeric phase.
    [0013] According to a preferred embodiment, the sacrificial polymeric phase (C) represents at least 15% by weight, preferably from 20 to 80% by weight of the total mass of the mixture of the step at).
    [0014] According to a preferred embodiment, step a) is carried out in an internal mixer or in an extruder. According to a preferred embodiment, step c) is carried out by thermal decomposition of the sacrificial polymeric phase.
    [0015] According to a preferred embodiment, the sacrificial polymeric phase is based on at least one polymer chosen from carbonate polyalkenes, preferably from carbonate polyethylenes and carbonate polypropylenes.
    [0016] According to a preferred embodiment, step b) comprises shaping in the form of a film. According to a preferred embodiment, the method further comprises at the end of step c) a step d) of compression.
    [0017] DETAILED DESCRIPTION The invention is based on a material comprising a porous thermally conductive composite material support comprising at least (A) a melt processable polymeric polymer phase and (B) thermally conductive fillers. This porous structure is partially or completely filled with at least one MCP in order to generate a thermal energy storage tank. This thermal storage material with high thermal conductivity, as well as high latent heat, has been achieved by a method employing conventional plastic transformation methods. In a first step, a thermally conductive material is produced. This material has a good mechanical cohesion thanks to the use of a polymer phase as a binder, and a high thermal conductivity due to the presence of thermal conductive mineral charges. This material has controlled pore quantity, pore size and morphology through the use of a sacrificial phase (C). The porosity of this material is then completely or partially filled with a phase change material (PCM), which provides the thermal storage function. ICG70038 EN 3034775 8 This result has been obtained by means of a method for incorporating, directly into the melt and by conventional plastic transformation methods, very high levels of mineral or carbon conductive thermal charges in the final material. The composition is chosen with regard to the manufacturing process employed and the final application of the material. The method of the invention also makes it possible to orient the charges with a form factor, by relying on the implementation parameters and, if necessary, on an additional step of recompression. The process of the invention has made it possible to melt thermal conducting materials which contain a mineral or carbon charge content greater than 80% by mass without prior modification of the surface of the charges or use of coupling agent or solvent, these materials being usable in the state for filling with a PCM. The mixture, the dispersion and the homogeneous distribution of the binder polymer and of the sacrificial phase and of the various mineral or carbon fillers are ensured by the implementation of the melt process. A possible pyrolysis or graphitization of the binder polymer is possible in a second time to optimize the performance, depending on the intended application. The control of the porosity in terms of size, volume and morphology is ensured by controlling the mixing parameters (screw profile, etc.) during the implementation of the process. In a second step, the material may be subjected to a compression step which results in a reduction of the pore volume. The control of the porosity is adapted according to the intended application. In the present description, the term "polymer" refers to both homopolymers and copolymers. It includes polymer blends, oligomers, mixtures of monomers, oligomers and polymers. The expression "consists essentially of" followed by one or more characteristics means that, in addition to the components or steps explicitly listed, may be included in the process or material of the invention, components or steps that do not significantly modify the properties and features of the invention. - The porous thermally conductive composite material support The support porous thermally conductive composite material comprises a binder polymer phase and thermally conductive fillers. It is obtained by implementing a sacrificial phase.
    [0018] The polymeric binder phase: The porous composite material support of the invention consists in particular of a polymeric phase forming a binder and ensuring its cohesion. The polymeric deposit phase can be of any kind since it can be converted by the molten route and is compatible with the sacrificial phase chosen. The binder polymeric phase advantageously has a melting temperature of at least 20 ° C lower than the decomposition temperature of the sacrificial phase so as to allow the melt processing of the mixture. The binder polymeric phase is solid at room temperature (around 20-25 ° C) since it must be able to be shaped and will constitute the binder of the final material. Compatibility between the binder polymeric phase and the sacrificial polymeric phase is evaluated in a manner well known to those skilled in the art by mixing the materials melt and observing whether there is phase separation or whether the mixture is substantially homogeneous. To implement the process and obtain a satisfactory material it is necessary to avoid phase macroseparation between the binder polymer and the sacrificial polymer during the implementation, macroseparation which would result in the presence of a pure phase of undispersed polymer of size greater than a few tens of imn. For the realization of this mixture, various parameters allow, in a well known manner, to modulate the compatibility between the two phases. Examples include, but are not limited to: choice of equipment, such as screw profile; Proportion of phases; compatibilizing agent. Reference can be made to a general work such as: "Mixing and Compounding of Polymers Theory and Practice", 2nd edition, Ica Edition, Manas-Zloczower, which describes in detail the main knowledge of polymer blending. The choice of the two phases makes it possible to control the implementation of the process, but also the properties of the final porous composite support, such as its integrity, its porosity and its conformability. The nature of the material constituting the polymeric binder phase is chosen as a function of the final properties expected of the material, such as, for example, its plasticity and its mechanical properties.
    [0019] According to one embodiment of the invention, pyrolysable and / or graphitizable polymers are used in the binder polymer phase. After an additional step of pyrolysis or graphitization, these polymers make it possible to obtain carbonaceous materials having a thermal conductivity. The polymeric binder phase comprises polymers and optionally additives. Preferably, the polymers represent at least 75% by weight of the binder polymer phase, advantageously at least 90%. Advantageously, the polymers used in the process of the invention and used in the composition of the final material (before possible pyrolysis) are chosen from: thermoplastics, elastomers and elastomeric thermoplastics. Examples that may be mentioned include: polyacrylonitrile, polyolefins, halogenated polymers, acrylic polymers, acrylates, methacrylates, vinyl acetates, polyethers, polyesters, polyamides, aromatic polymers or else elastomeric polymers, for example hydrogenated acrylonitrile-butadiene (HNBR), copolymers of ethylene and an alkyl acrylate, polyisoprene or other rubbers.
    [0020] The binder polymer phase is based on at least one polymer selected from: thermoplastics, elastomers, thermoplastic elastomers, which means that thermoplastic polymers, elastomers and thermoplastic elastomers account for at least 95% by weight of polymers of the polymeric phase forming a binder, advantageously at least 98%.
    [0021] According to a preferred embodiment of the invention, the polymeric binder phase comprises at least 50%, preferably at least 90%, more preferably at least 95% by weight of at least one polymer selected from polyacrylonitrile, 1 hydrogenated acrylonitrile-butadiene and mixtures thereof Among the additives which may be used in the binder polymer phase, there may be mentioned additives which are chosen for their function in the final material, for example: agents which improve the resistance to fire or oxidation or still crosslinking agents, such as bifunctional organic compounds, organic peroxides or sulfur compounds (for the crosslinking of rubbers), co-agents such as tri-allyl cyanurate. The use of these additives is useful without being necessary to the invention and depends directly on the intended application. The sacrificial polymeric phase: The sacrificial polymeric phase is composed of materials which have the property of decomposing during the application of a chosen external stress, such as for example by raising the temperature or by dissolving in a solvent. The elimination or extraction of the sacrificial phase must be able to be implemented without impacting the rest of the material. It is preferable to use as a sacrificial material a compound leaving little or no residue during decomposition. In the context of the present invention, the presence of small amounts of sacrificial material in the pores of the porous composite support can improve the wettability of this support and thus facilitate its filling by the MCP. Advantageously, the sacrificial polymeric phase is solid at ambient temperature (around 20-25 ° C.) so as to allow the composition to be shaped. Preferably, a sacrificial phase which can be extracted by thermal decomposition is chosen, and polymers with a known degradation temperature of the literature are preferred, ensuring that the degradation temperature of the sacrificial phase is lower by at least 20 ° C relative to the degradation temperature of the polymer (s) chosen (s) for the polymeric phase binder. Among the polymers which can be removed by raising the temperature, mention may be made of carbonate polyalkenes, such as, for example, carbonate polyethylenes and carbonate polypropylenes. Generally, these materials have the advantage of decomposing with a moderate or no volume expansion. Thus, the volume of the shaped part is not or only slightly affected by the step of decomposition of the sacrificial phase. In the presence of certain fillers such as graphite, the use of carbonate polyalkenes can nevertheless sometimes lead to volume expansion. To improve the fluidity of the intermediate polymeric material and to facilitate the implementation of the process, in a manner known to those skilled in the art, it is possible to use a mixture of carbonate polyalkenes of different molar masses.
    [0022] According to another embodiment, the sacrificial polymeric phase may be extracted with a solvent and is based on at least one liquid-extractable sacrificial polymer, preferably chosen from: polyethylene glycols, polypropylene glycols and mixtures thereof. The sacrificial polymeric phase comprises polymers and optionally additives. Preferably, the polymers represent at least 95% by weight of the sacrificial polymeric phase, advantageously at least 98%. Advantageously, the sacrificial polymeric phase is based on at least one polymer chosen from carbonate polyalkenes, which means that the carbonate polyalkenes represent at least 95% by weight of the sacrificial polymer phase, advantageously at least 98%. According to a preferred embodiment of the invention, the carbonate polyethylenes and the carbonate polypropylenes represent at least 95% by weight of the sacrificial polymeric phase, advantageously at least 98%. Among the additives that may be used in the sacrificial polymeric phase, mention may be made of photoacid generators which act as additives to aid the decomposition of the sacrificial phases. Such products are described in Cupta M., Jayachandran P., Khol P., Photoacid Generators for Catalyst Decomposition ICG70038 DE 3034775 12 of Polycarbonate, Journal of Applied Polymer Science, 2007, Vol. 105, p.2655-2662, for polypropylene carbonate for example. The use of these photoacids in the sacrificial polymeric phase makes it possible to reduce the degradation temperatures. They are therefore useful without being necessary to the invention.
    [0023] The fillers According to the invention, use is made in the porous composite material support of the invention of thermal conductive fillers. The thermally conductive filler is advantageously chosen from those having a thermal conductivity greater than or equal to 5 W / mK.
    [0024] The intrinsic thermal conductivity of known fillers is described, for example, in "Thermal Conductivity of Nonmetallic Solids," YS Touloukian, RW Powell, CY Ho, and PG Klemans, IFI / Plenum: New York-Washington, 1970, or in "Thermal Conductivity. Theory, Properties and Applications, "TM Tritt, Ed., Academic Kluwer / Plenum Publishers: New York, 2004.
    [0025] Preferably, the thermally conductive filler has an intrinsic thermal conductivity greater than or equal to 10 W / mK, more preferably greater than or equal to 25 W / mK, advantageously greater than or equal to 50 W / mK. Thermally conductive fillers that can be used in the invention are, for example: AlN (aluminum nitride), BN (boron nitride), MgSiN 2 (magnesium and silicon nitride), SiC (silicon carbide) , graphite, graphene, carbon nanotubes (CNT), carbon nanofibers, carbon black, diamond, metal fillers such as aluminum, copper or silver or a combination thereof. It should be emphasized that some of these fillers, such as metal fillers, graphite, graphene, carbon nanotubes (CNTs), carbon nanofibers, carbon black, can also be electrically conductive. When it is desired to obtain an electrically insulating material, it is avoided to use such charges. In this case, a filler having a resistivity greater than or equal to 103 Ohm.cm is preferably used, such as aluminum nitride, boron nitride, magnesium and silicon nitride or silicon carbide. Additives: In addition to the additives intended to modify the properties of the support made of porous composite material, and those intended to facilitate the elimination of the sacrificial phase, it is possible to add specific additives to the composition in order to improve and / or Optimize the material manufacturing process, such as compatibilizing agents. These additives facilitating the implementation of the process may be incorporated beforehand in one or the other of the polymer phases, or with the fillers, or they may be incorporated independently. The process for preparing a porous composite material support: The process of the invention is based on the use of a sacrificial polymeric phase in a melt process, allowing both a plasticization, a better fluidity of the material during processing and melt cohesion but also the creation of a controlled porosity. For example, an open porosity can be sought to reduce the density of the material while ensuring a high thermal conductivity and the ability to incorporate a continuous MCP phase. The porosity can be controlled directly by the amount of sacrificial material introduced or by a possible compression of the material after shaping and elimination of the sacrificial phase. It should be noted that the process according to the invention allows both short process times, typical of conventional plastic processing processes, such as extrusion, but also the use of steps requiring melt cohesion. like extrusion calendering. It must also be emphasized that the capacity of the mixture to be converted is maintained after shaping, as long as no extraction or pyrolysis has been carried out. This process comprises the following steps: a) Melt melt mixing of the binder polymeric phase (A), fillers (B), and the sacrificial polymeric phase (C) to form a mixture, b) Mixing of the mixture, c) Elimination of the sacrificial polymeric phase. Step a) can be carried out in a known manner in any type of equipment that makes it possible to homogenize the composition while heating it. There may be mentioned an internal mixer or an extruder. Compared to the previous methods, the method of the invention has many advantages, and in particular the mixing step is carried out without solvent. The binder polymeric phase is homogeneously dispersed in the continuous sacrificial polymeric phase, or it forms a co-continuous phase with the latter. To facilitate obtaining a homogeneous mixture, it is possible, for example, to use the sacrificial polymeric phase in the form of granules of average size in a number greater than 1 mm. The heating is controlled so as to bring the polymer phases to melt without decomposing the sacrificial phase or at a temperature at which the sacrificial phase decomposes very slowly (over a period greater than 1 hour). Advantageously, the heating in step a) is controlled to bring the mixture to a temperature at least 20 ° C higher than the glass transition temperature or melting of the polymers of the polymeric binder phase. The shaping step is adapted according to the final shape and the dimensions that one wishes to confer on the object. The shaping may consist, for example, of one or more steps selected from: extrusion, blowing, injection, molding, calendering, kneading and combinations thereof. An advantage of the process of the invention lies in the possibility, when using fillers with a form factor, to orient these charges. The creation of a porosity contributes in itself to the orientation of these charges. Furthermore, the passage 10 through an extrusion die under selected pressure conditions allows to give an orientation to such loads. Compression and / or calendering can also contribute to the orientation of the loads. Such a charge orientation in the porous composite material results in an asymmetry of properties, and increases the thermal conductivity properties in one direction of the material. The method of the invention also makes it possible to obtain objects of various shapes, self-supporting, and not only coatings attached to a support. At the end of steps a) or b), a polymeric composition is obtained which is an intermediate composition of the process of the invention. It may be in the molten state or already shaped. It is a precursor of the porous composite support. This composition comprises at least: (A) a melt-processable polymer phase, advantageously based on polymers chosen from thermoplastic polymers, elastomers and elastomer thermoplastics, (B) a filler chosen from thermal conductive fillers (C) a sacrificial polymeric phase. Advantageously in this composition, the charges (B) represent at least 50%, preferably at least 70%, more preferably at least 80% by weight relative to the sum of the masses of the polymer (A) and the charges (B).
    [0026] Advantageously in this composition, the sacrificial polymeric phase (C) represents at least 15% by weight relative to the sum of the masses of (A), (B) and (C). Advantageously, the polymeric composition comprises, or better consists essentially of, by weight relative to the total mass of the composition: (A) 1 to 15% of polymer phase based on polymers chosen from thermoplastic polymers, elastomers and 30 to 70% of charge (s) selected from among the thermal conductive fillers, (C) 20 to 80% of sacrificial polymeric phase. This polymeric composition can be prepared and shaped directly into the desired form for use (film, casing, etc.). Alternatively, there is provided an embodiment where the composition is prepared (homogeneous melt mixture of components (A), (B) and (C)) and granular form for example. This composition is then easily reintroduced into the process of the invention in step a). This embodiment makes it possible to provide a ready-to-use composition which does not require dosing of the components and avoids handling errors related to the introduction of the components into the mixer. The sacrificial polymeric phase is removed after shaping the composite polymer composition substantially without leaving any residue. This step can be carried out in a known manner by raising the temperature, for example in an oven. It can also be carried out by other means, for example by dissolving the sacrificial phase with the aid of a solvent. In addition to the steps described above, the method of the invention may comprise other steps. In particular, according to one embodiment of the invention, it comprises one or more shaping steps at the end of step c), and in particular a cutting of the material to the desired dimensions, a compression which makes it possible to reduce porosity. The compression can for example be carried out by means of a platen press or by calendering. Possible crosslinking of the binder phase is possible to optimize the mechanical properties and the cohesion of the composition if further processing is not envisaged. Advantageously, the porous composite material support comprises, or better consists essentially of, in mass relative to the total mass of the support: 3 to 40% of at least one polymer chosen from thermoplastic polymers, elastomers and thermoplastic elastomers, 30 - 60 to 97% of at least one filler selected from thermal conductive fillers, 0 to 5% of one or more additives, or decomposition residues of the sacrificial phase. Preferably, the porous composite material support comprises, or preferably consists essentially of, by weight relative to the total mass of the support: 3 to 20% of at least one polymer chosen from thermoplastic polymers, elastomers and thermoplastics Elastomers, ICG70038 EN deposit 3034775 16 - 80 to 97% of at least one charge selected from thermal conductive fillers, 0 to 2% of one or more additives, or decomposition residues of the sacrificial phase.
    [0027] Even more preferably, the porous composite material support comprises, or better consists essentially of, in mass relative to the total mass of the support: 4 to 10% of at least one polymer chosen from thermoplastic polymers, elastomers and elastomeric thermoplastics, 10 - 90 to 96% of at least one filler chosen from thermal conductive fillers, 0 to 1% of one or more additives, or sacrificial phase decomposition residues, According to one embodiment of the invention, the support of porous composite material comprises, or better consists essentially of, in mass relative to the total mass of the support: - 3 to 40% of at least one polymer chosen from polyacrylonitrile, polyolefins, halogenated polymers, acrylic polymers, acrylates, methacrylates, vinyl acetates, polyethers, polyesters, polyamides, aromatic polymers, acrylonitrile-butadiene hydrogenated copolymers of ethylene and an alkyl acrylate, polyisoprene, rubbers, - 60 to 97% of at least one filler selected from aluminum nitride, boron nitride, nitride of magnesium and silicon, silicon carbide, diamond, and mixtures thereof, 25 - 0 to 5% of one or more additives, or decomposition residues of the sacrificial phase. Advantageously, the porous composite material support comprises, or better consists essentially of, in mass relative to the total mass of the support: 3 to 20% of at least one polymer chosen from polyacrylonitrile, polyolefins and halogenated polymers , acrylic polymers, acrylates, methacrylates, vinyl acetates, polyethers, polyesters, polyamides, aromatic polymers, hydrogenated acrylonitrile-butadiene, copolymers of ethylene and an alkyl acrylate, polyisoprene, rubbers, 80 to 97% of at least one filler selected from: aluminum nitride, boron nitride, magnesium and silicon nitride, silicon carbide, diamond, and mixtures thereof , ICG70038 DE deposit 3034775 17 - 0 to 2 ° A of one or more additives, or of decomposition residues of the sacrificial phase. According to a preferred embodiment of the invention, the porous composite material support comprises, or better consists essentially of, by mass relative to the total mass of the support: 4 to 10% of at least one polymer chosen from polyacrylonitrile, polyolefins, halogenated polymers, acrylic polymers, acrylates, methacrylates, vinyl acetates, polyethers, polyesters, polyamides, aromatic polymers, hydrogenated acrylonitrile-butadiene, ethylene copolymers and an alkyl acrylate, polyisoprene, rubbers, 90 to 96% of at least one filler chosen from: aluminum nitride, boron nitride, magnesium and silicon nitride, carbide silicon, diamond, and mixtures thereof, 0 to 1% of one or more additives, or decomposition residues of the sacrificial phase. Advantageously, this support is obtained at the end of the process described above. The support of porous composite material of the invention has high thermal conductivity properties, due to the presence of thermal conductive fillers in significant proportion. The porous composite material backing of the invention has porosity and density that can be controlled. Indeed, several parameters of the process make it possible to modify these properties of the material: the proportions of the initial mixture of (A), (B), (C) and possibly the shaping mode, a possible compression step. The porosity can thus be controlled in terms of size, morphology and pore quantity. Depending on the applications and the constraints related to the use, one chooses to favor a higher or lower density of the support. By support in porous composite material is meant a material of which at least 1% by volume, advantageously at least 10% by volume, consists of pores. Advantageously, the support of the invention has a continuous porosity.
    [0028] According to one embodiment of the invention, the porosity represents from 10 to 70% by volume relative to the total volume of the material, preferably from 20 to 60%. Preferably, a fine porosity is preferred which makes it possible to retain the MCP in the pores of the support, even when it is in the liquid state. In addition, MCPs being non-thermal conductors, their presence in the material reduces the thermal conductivity thereof. The choice of a fine porosity makes it possible to reduce the influence of the MCP on the thermal conductivity of the material filled with MCP. The material is shaped according to the intended use, especially in the form of sheets, films, but also ducts, cables, coatings, granules, housings. For example, the method of the invention provides access to spherical porous composite supports which, once porosity is filled by MCP, can be used for energy storage. Advantageously, the porous composite material support is self-supporting. Compared to the supports obtained by the solvent route, which can also be porous, the material of the invention has the advantage of being able to present various shapes, of significant thickness. Indeed, by solvent, we have access to materials in the form of films of a few hundred microns maximum thickness, while the materials of the invention can be of all shapes and sizes. In the case where the material of the invention is in the form of a film, it is advantageously of a thickness greater than or equal to 250 μm, preferably greater than or equal to 500 μm, advantageously still greater than or equal to 1 mm, even better, greater than or equal to 2.5 mm. The material of the invention is advantageously characterized in that it has in all directions of space a thickness greater than or equal to 250 μm, preferably greater than or equal to 500 μm, advantageously still greater than or equal to 1 mm.
    [0029] The thermal composite materials supports of the invention have a combination of interesting properties: they are both porous and have a high thermal conductivity. The phase change material The phase change materials have the ability to change their physical state within a certain temperature range. When the melting temperature is reached by heating, the phase change takes place from the solid state to the liquid state. During this melting process, the phase change material absorbs and stores a large amount of latent heat. The temperature of the phase change material remains substantially constant throughout the process. In a method of cooling a phase change material, within a certain temperature range, the stored heat is released into the environment, and a reverse phase change from the liquid state to the solid state occurs. . During this crystallization process, the temperature of the phase change material also remains constant. The interest of phase change materials as a source of heat storage is based on the heat transfer during the melting process and the crystallization process. Many phase change materials are known, they differ in their temperature change ranges and their energy storage capabilities. These materials can be used individually or mixed to modulate their phase change temperature ranges.
    [0030] For example, mention may be made of: hydrogen carbonate chains, such as henicosane, eicosane, nonadecane, octadecane, heptadecane and hexadecane. It may also be mentioned: hydrated salts such as calcium chloride hexahydrate, lithium nitrate trihydrate, sodium sulfate decahydrate. There may also be mentioned liquid solvents at room temperature, such as water, ethanol, acetone. Preferably, a PCM is used with a liquid / solid phase transition (DSL) rather than liquid / gas (L / G): on the one hand, the L / S transition is reversible and, on the other hand, it allows better check for possible expansion of the material. Preferably, a PCM is used which has a lower phase transition temperature of at least 20 ° C than the degradation temperature of the binder polymeric phase. The phase-change material is introduced into the porous composite support by impregnation, for example the porous composite support is immersed in the MCP in the liquid state and then removed and cooled, which makes it possible to obtain a complete filling or almost complete porosity of the support. In a manner known to those skilled in the art, the material of the invention is characterized for its energy storage properties by differential scanning calorimetry or DSC (Differential Scan Calorimetry). Advantageously, the MCP fills at least 50%, preferably at least 70%, more preferably at least 85% by volume relative to the total volume of the porosity of the porous composite material support. An advantage of the material of the invention over prior art materials, especially crosslinked materials, is that it is transformable and can be recycled. For example, the MCP phase of the material can be removed to recover the porous composite material support. It is then possible to introduce, in step a) of the process described above, the support made of porous composite material recovered from polymer and fillers, by adding to it a new sacrificial phase, optionally other polymers and additional fillers, and proceeding thus to a new cycle of transformation.
    [0031] The material of the invention can be used in many applications such as: Heat sink in an electronic equipment (heat sink), storage medium ICG70038 EN 3034775 storage medium of energy produced by intermittent renewable energy sources such as solar batteries or wind turbines. According to one variant, the invention relates to a process for producing a porous carbonaceous material which is heat conducting, this process comprising the production of a porous carbon support comprising at least one (A) a polymeric phase and (B) one or more fillers selected from heat conductive fillers; - partially or completely filling the porosity of the porous carbon carrier with at least one phase change material, wherein the manufacturing of the porous carbon carrier comprises the following steps a) Melt hot melt of the polymeric phase (A), the fillers (B), and a sacrificial polymeric phase (C), so as to obtain a mixture, b) Formatting the mixture, c) Elimination of the sacrificial polymeric phase, d) Pyrolysis or graphitization. Advantageously, the same characteristics as those described above for steps a), b) and c) as well as for the proportions of the components are implemented. In known manner, the pyrolysis treatment is carried out at a temperature greater than or equal to 500 ° C, the graphitization treatment at a temperature greater than or equal to 1000 ° C. For this, the choice of the polymeric phase forming binder must have been adapted to allow this step. A composite carbonaceous material having a high amount of thermal conductive fillers and controlled porosity and density is thus obtained. Such a material can be used as energy storage material in the following applications: encapsulation of electronic components, battery boxes, electrical cabinets, servers.
    [0032] Experimental part: Materials and methods: 1.1 Materials: Binder polymer: PL 1: polyacrylonitrile sold by the company Ineos under the reference Barex 210 e PL2: HNBR elastomer (hydrogenated acrylonitrile-butadiene) sold by the company Zeon Chemicals under the reference Sacrificial polymer: PS 1: polypropylene carbonate marketed by Novomer under the reference Polyol 211-10 ® PS 2: polypropylene carbonate marketed by the company Empower Materials 5 under the reference QPAC40 ® Heat conducting charge: Cl: Graphite marketed by the company Timcal under the reference C-therm 001 0 C2: Aluminum nitride 10 Material with phase change: MCP1: Eicosane Extruder: Coperion ZSK18 Internal mixer: Scamex 300 ml 1.2. Test Methods and Characterization: Thermal Conductivity: The materials were characterized at room temperature and in the plane by the thin plate TPS hotdisk method by following the NI IS022007-2: 200812 plastic standard. Density: To assess the density, the mass of the material was measured on a precision scale and caliper volume, all at room temperature. Differential Scanning Calorimetry (DSC): Enthalpies were measured on a Mettler branded instrument at -20 ° C to 100 ° C at a rise rate of 5 ° C / minute.
    [0033] II. Polymeric compositions and composite materials: In the composition tables, the "Before extraction" columns describe the proportions of the composition before step c) of elimination of the sacrificial phase, the "After extraction" columns describe the material obtained after step c). 11.1 Example 1 II.1.A Preparation of the Porous Composite Support: Formulation: A mixture having the following composition was prepared: Deposition prior to extraction Composition% mass% volume PL1 13.2 17.4 PS1 13.8 16.5 PS2 19.8 23.8 Cl 53.2 Table 1.1 Method of preparation: After extraction% mass% volume 19.9 29.1 - Step a: Preparation of the composition and extrusion of a film of composite material The composition was prepared using a twin-screw extruder at 175 ° C. All raw materials were directly injected into the extruder using gravimetric feeders for powders and granules, and an injection needle for liquids. The mass flow rates of each component were adjusted to obtain the composition described above. Step b: Shaping Using a gear pump following the twin-screw extruder, films of 2 mm thickness were continuously extruded. The film was cut into samples of dimensions 5 cm x 5 cm. Step c: Elimination of the sacrificial phase The previously obtained film sample was subjected to a decomposition step of the sacrificial phase in an oven under air at 230 ° C. for 20 minutes. Measuring the mass difference before and after the heat treatment makes it possible to monitor and control the removal of the polypropylene carbonate. 100% of the polypropylene carbonate initially incorporated into the mixture is decomposed and removed. A porous material is obtained consisting of polymer forming PL1 binder and Cl charge in the proportions of Table 1.1, and whose porosity is about 40% by volume relative to the total volume of the material. Properties: The thermal conductivity of the resulting material is 12.5W / m ° K.
    [0034] II. 1.B Filling the porous composite support with a PCM: Formulation: The porous composite support obtained was immersed in liquid eicosane so that it filled the porosity. The material was then removed from the solution and cooled. Mass measurements were made before and after contact with eicosane. As a result, after calculation related to the density, 100% of the initial porosity was filled by eicosane giving a new composition shown in Table 1.2: Composition% mass% vol PL1 15.0 17.2 Cl 60.3 41.7 MCP 1 24.7 Table 1.2 Properties: The material of Table 1.2 was then characterized by DSC at 1 and 5 ° C / min by rising in temperature (melting) and falling in temperature (crystallization) between 10 0 and 100 ° C to determine the temperature. stored enthalpy and reversibility. An enthalpy of fusion of 80 J / g at 5 ° C./min. This spreads over a range of 10 ° C with a beginning of melting at 36 ° C and a peak at 41 ° C. 11.1 Example 2 II.2.A Preparation of the porous composite support: Formulation: A mixture having the following composition was prepared: Composition% mass After extraction% volume% mass% volume Before extraction PL2 3.7 5.9 6.1 11.3 1 PS1 25.1 30.7 0 Table 2.1 Method of Preparation: Step a: Preparation of the Composition and Formation of a Film of Composite Material The composition was prepared using an internal mixer at 80 ° C. The binder polymer PL2 and the sacrificial polypropylene PS2 were introduced and blended first to obtain a plasticized melt blend. Then the mineral fillers C1 were added gradually with regular addition of the sacrificial polymer PS1 (a preheating, at about 60 ° C., of the material may be necessary in order to reduce the viscosity and facilitate the addition) until a homogeneous mixture. Step b: Shaping The mixture obtained previously was then calendered in the form of a sheet of thickness 0.5 cm. The resulting film was cut into samples of dimensions 5 cm x 5 cm. Step c: Removal of the sacrificial phase The previously obtained film sample was subjected to a decomposition step of the sacrificial phase in an oven under air at 230 ° C for 20 minutes. Measuring the mass difference before and after the heat treatment makes it possible to monitor and control the removal of the polypropylene carbonate. 100% of the polypropylene carbonate initially incorporated into the mixture is decomposed and removed. A volume expansion of the material is observed during this step. A porous material is obtained consisting of polymer forming PL2 binder and Cl charge in the proportions of Table 2.1. Step d: Compression The mixture is compressed in a press at 80 ° C and 50 bar to a film thickness of 0.5 cm so as to recover the original thickness. Indeed, during the decomposition there is a slight swelling of the mixture. The compression material has a density of 0.844 g / cm 3 instead of 1.80 g / cm 3 theoretical (the theoretical density is calculated from the formulation and density of each element). It is deduced from the measurement of the density that the material has a porosity of 53% by volume relative to the total volume of the material. Properties: At the end of step d, the thermal conductivity of the material was measured in the radial direction and in the axial direction. The thermal conductivities obtained are reported in Table 2.2. ICG70038 EN deposition 3034775 25 Sens Thermal Conductivity (W / m.K) Radial 16.0 Axial 1.49 Table 2.2 It can be seen that the material obtained has several properties: a high thermal conductivity, a charge orientation and a low density. II.2.B Filling the porous composite support with a PCM: Formulation: The material was dipped in liquid eicosane so that it filled the porosity. The material was then removed from the solution and cooled. Mass measurements were made before and after contact with eicosane. As a result, after density calculation, about 90% of the initial porosity has been filled by the eicosane giving a new composition shown in Table 2.3: Composition% mass% vol PL2 8.2 6 Cl 63.9 47.1 MCP Table 2.3 Properties: The material of Table 2.3 was then characterized by DSC at 1 and 5 ° C / min, rising in temperature (melting) and falling in temperature (crystallization) between 0 and 100 ° C. in order to determine stored enthalpy and reversibility. An enthalpy of fusion of 85 J / g at 5 ° C./min. This spread over a range of 10 ° C with a beginning of melting at 36 ° C and a peak at 39 ° C. 11.3 Example 3 11.3 .A Preparation of the porous composite support: Formulation: A mixture having the following composition ("Before extraction" column) was prepared: Deposit 3034775 26 15.0 5.0 Before extraction% vol 9.0 20.0 20.0 After extraction% mass% vol Composition PL2 PS1 PS2 Table 3.1 Method of preparation: Step a: Preparation of the composition and formation of a film of composite material 5 was performed as in step a of Example 2. - Step b: Shaping The mixture obtained was then calendered in the form of a 1 cm thick sheet. Step c: Removal of the sacrificial phase The procedure was as in step c of Example 2. No volume expansion of the material during this step should be noted. A porous material consisting of polymer forming PL2 and C2 filler is obtained in the proportions of Table 3.1. Properties: During the heat treatment, the polypropylene carbonate starting material was measured by mass difference. 100% of the polypropylene carbonate initially incorporated in the mixture is decomposed. II.3.B Filling the porous composite support with a PCM: Formulation: The material was dipped in liquid eicosane so that it filled the porosity. The material was then removed from the solution and cooled. Mass measurements were made before and after contact with eicosane. As a result, after calculation related to the density, about 90% of the initial porosity has been filled by eicosane giving a new composition shown in Table 3.3: Composition% mass% vol PL2 4.2 9.1 C2 80.7 1 51.3 MCP 1 15.1 Table 3.3 Properties: The material of Table 3.3 was then characterized by DSC at 1 and 5 ° C / min by rising in temperature (melting) and falling in temperature (crystallization) between 5 0 and 100 ° C to determine stored enthalpy and reversibility. An enthalpy of fusion of 45 J / g at 5 ° C./min. This spread over a range of 10 ° C with a beginning of melting at 39 ° C and a peak at 41 ° C.
    权利要求:
    Claims (16)
    [0001]
    REVENDICATIONS1. Material comprising: a support made of a porous composite material comprising at least (A) a binder-forming polymer phase based on at least one polymer chosen from thermoplastic polymers, elastomers and elastomer thermoplastics, and (B) one or more fillers chosen from among the thermal conductive fillers, the pores of the support made of porous composite material being partially or completely filled with: at least one phase-change material.
    [0002]
    2. Material according to claim 1, wherein the conductive thermal charges (B) represent at least 60% by weight relative to the sum of the masses of the polymeric phase (A) and the charges (B).
    [0003]
    3. The material of claim 1 or claim 2, wherein the phase change material forms a continuous phase in the porosity of the porous composite material support. 20
    [0004]
    4. Material according to any one of the preceding claims, wherein the polymeric binder phase is based on at least one polymer chosen from: polyacrylonitrile, polyolefins, halogenated polymers, acrylic polymers, acrylates, methacrylates vinyl acetates, polyethers, polyesters, polyamides, aromatic polymers, hydrogenated acrylonitrile-butadiene, copolymers of ethylene and an alkyl acrylate, polyisoprene, rubbers.
    [0005]
    5. Material according to any one of the preceding claims, in which the fillers are chosen from: aluminum nitride, boron nitride, magnesium and silicon nitride, silicon carbide, diamond, graphite , graphene, carbon nanotubes (CNT), carbon black, metal fillers such as aluminum, copper or silver, and mixtures thereof. 35
    [0006]
    6. Material according to any one of the preceding claims, wherein the porosity is at least 40% by volume relative to the total volume of the porous composite material support. 3034775 ICG70038 EN reply notification 10 07 15 29
    [0007]
    The material of any of the preceding claims, wherein the phase change material is selected from hydrocarbon chains.
    [0008]
    8. A method of manufacturing a material according to any one of claims 1 to 7 comprising: - the manufacture of a porous composite material support comprising at least (A) a polymeric phase and (B) one or more selected fillers among the thermal conductive fillers, - The partial or total filling of the porosity of the porous composite material support with at least one phase-change material.
    [0009]
    9. The method of claim 8 wherein the manufacture of the support of porous composite material comprises the following steps: a) Melt hot melt of the polymeric phase (A), charges (B), and a polymeric phase sacrificial (C), so as to obtain a mixture, b) shaping of the mixture, c) elimination of the sacrificial polymeric phase. 20
    [0010]
    10. The method of claim 9, wherein the sacrificial polymeric phase (C) is at least 15% by weight, preferably 20 to 80% by weight of the total mass of the mixture of step a). 25
    [0011]
    11. Process according to any one of claims 9 to 10 wherein step a) is carried out in an internal mixer or in an extruder.
    [0012]
    12. A process according to any one of claims 9 to 11 wherein step c) is carried out by thermally decomposing the sacrificial polymeric phase.
    [0013]
    13. The method of claim 12 wherein the sacrificial polymeric phase is based on at least one polymer selected from carbonate polyalkenes, preferably from carbonate polyethylenes and polypropylenes carbonates.
    [0014]
    14. A method according to any one of claims 9 to 13 wherein step b) comprises shaping in film form. 3034775 ICG70038 EN reply notification 10 07 15 30
    [0015]
    15. Method according to any one of claims 9 to 14 which further comprises at the end of step c) a step d) of compression. 5
    [0016]
    16. Use of the material according to any one of claims 1 to 7, or the material obtained by the method according to any one of claims 8 to 15 in one of the following applications: - heat sink in electronic equipment, - energy storage medium. 10
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    同族专利:
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    WO2016165999A1|2016-10-20|
    CN107646044A|2018-01-30|
    US20180094180A1|2018-04-05|
    CN107646044B|2022-01-07|
    FR3034775B1|2018-09-28|
    CA2981655A1|2016-10-20|
    EP3283594A1|2018-02-21|
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    优先权:
    申请号 | 申请日 | 专利标题
    FR1553213|2015-04-13|
    FR1553213A|FR3034775B1|2015-04-13|2015-04-13|MATERIAL FOR THERMAL STORAGE|FR1553213A| FR3034775B1|2015-04-13|2015-04-13|MATERIAL FOR THERMAL STORAGE|
    US15/566,273| US20180094180A1|2015-04-13|2016-04-07|Heat storage material|
    PCT/EP2016/057554| WO2016165999A1|2015-04-13|2016-04-07|Heat storage material|
    JP2017553213A| JP6785790B2|2015-04-13|2016-04-07|Heat storage material|
    CN201680029712.3A| CN107646044B|2015-04-13|2016-04-07|Heat storage material|
    EP16718223.7A| EP3283594B1|2015-04-13|2016-04-07|Heat storage material|
    CA2981655A| CA2981655A1|2015-04-13|2016-04-07|Heat storage material|
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