WO2016088682A1 - 熱伝導シート及びその製造方法 - Google Patents
熱伝導シート及びその製造方法 Download PDFInfo
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- WO2016088682A1 WO2016088682A1 PCT/JP2015/083450 JP2015083450W WO2016088682A1 WO 2016088682 A1 WO2016088682 A1 WO 2016088682A1 JP 2015083450 W JP2015083450 W JP 2015083450W WO 2016088682 A1 WO2016088682 A1 WO 2016088682A1
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Definitions
- the present invention relates to a heat conductive sheet having excellent heat conductivity and a method for producing the heat conductive sheet.
- Patent Document 1 discloses an expanded graphite sheet made only of expanded graphite.
- the thermal conductivity in the surface direction is 350 W / m ⁇ K or more.
- Patent Document 2 discloses a graphite sheet laminate in which a metal material is sandwiched between graphite sheets.
- the said graphite sheet laminated body is produced by arranging a metal material between graphite sheets and rolling.
- Patent Document 3 discloses a high thermal conductive member in which metal compound particles are dispersed in an oriented graphite structure.
- JP 2006-62922 A Japanese Patent Laid-Open No. 11-240706 JP 2005-119887 A
- the graphite sheet laminated body of patent document 2 since the graphite sheet is rolled in the manufacturing process, the graphite is oriented in the plane direction. Therefore, even if a sheet having high thermal conductivity is arranged between the graphite sheets, the thermal conductivity in the thickness direction is still not sufficient.
- the high thermal conductivity member of Patent Document 3 obtains high thermal conductivity by mixing the thermal conductive particles while maintaining the orientation of graphite, but the thermal conductivity in the thickness direction is still insufficient. .
- An object of the present invention is to provide a heat conductive sheet and a method for producing the heat conductive sheet, which are excellent in thermal conductivity in the thickness direction of the sheet.
- the thermally conductive sheet according to the present invention is a thermally conductive sheet, and includes expanded graphite and orientation control particles, and at least a part of the expanded graphite is defined as the sheet surface direction due to the presence of the orientation control particles. Oriented in different directions.
- the expanded graphite is oriented in the thickness direction of the sheet due to the presence of the orientation control particles.
- the thermal conductive sheet according to the present invention preferably has a thermal conductivity in the thickness direction of 5 W / m ⁇ K or more.
- the weight ratio of the expanded graphite to the orientation control particles is preferably in the range of 1/4 or more and 5 or less.
- the heat conductive sheet according to the present invention preferably has a specific gravity in the range of 1.5 g / cm 3 or more and 5 g / cm 3 or less.
- the expanded graphite may be partially exfoliated exfoliated graphite having a structure in which graphene is partially exfoliated.
- Orientation control particles may be included in the partially exfoliated exfoliated graphite.
- the orientation control particles are an inorganic compound.
- the orientation control particles preferably have an average particle size of 0.2 ⁇ m or more and 1000 ⁇ m or less.
- the method for producing a heat conductive sheet according to the present invention is a method for producing a heat conductive sheet, comprising preparing a mixture of expanded graphite and orientation control particles, and forming the mixture into a sheet by pressing, Orienting at least a part of the expanded graphite in a direction different from the sheet surface direction.
- the expanded graphite and the orientation control particles are mixed in the presence of a supercritical medium.
- the sheet molding is performed by filling the mixture in a cylinder and pressing the mixture.
- the heat conductive sheet according to the present invention includes expanded graphite and orientation control particles as described above. Further, at least a part of the expanded graphite is oriented in a direction different from the sheet surface direction due to the presence of the orientation control particles. Therefore, the heat conductive sheet which concerns on this invention is excellent in the heat conductivity in the thickness direction of a sheet
- FIG. 1 (a) is an SEM photograph at a magnification of 600 times of the cross section of the heat conductive sheet obtained in Example 1.
- FIG. FIG. 1B is an element mapping image of the SEM photograph of FIG.
- FIG. 2A is an SEM photograph with a magnification of 2000 times of the cross section of the heat conductive sheet obtained in Example 1.
- FIG. 2B is an element mapping image of the SEM photograph of FIG.
- FIG. 3A is a SEM photograph of 1000 times the cross section of the heat conductive sheet obtained in Comparative Example 1.
- FIG. 3B is an element mapping image of the SEM photograph of FIG.
- the heat conductive sheet according to the present invention includes expanded graphite and orientation control particles. At least a part of the expanded graphite is oriented in a direction different from the surface direction of the sheet due to the presence of the orientation control particles. Therefore, the heat conductive sheet which concerns on this invention is excellent in the heat conductivity in the thickness direction of a sheet
- At least a part of the expanded graphite is preferably oriented in the thickness direction of the sheet due to the presence of the orientation control particles. In that case, the thermal conductivity in the thickness direction of the sheet can be more effectively increased.
- the thermal conductivity in the thickness direction of the heat conductive sheet is preferably 5 W / m ⁇ K or more, more preferably 7 W / m ⁇ K or more, and even more preferably 10 W / m ⁇ K or more.
- the heat conductivity in the thickness direction is not less than the above lower limit, the heat dissipation property of the heat conductive sheet can be further enhanced.
- the upper limit of the thermal conductivity in the thickness direction of the thermal conductive sheet is not particularly limited, and can be set to be equal to or lower than the thermal conductivity when the expanded graphite is completely oriented in the thickness direction.
- the specific gravity of the heat conductive sheet is preferably 1.5 g / cm 3 or more, more preferably 1.6 g / cm 3 or more, further preferably 1.7 g / cm 3 or more, and may exceed 2.0 g / cm 3. Particularly preferred.
- As the specific gravity of the heat conducting sheet is preferably 5 g / cm 3 or less, more preferably 3g / cm 3, 2.5g / cm 3 or less is more preferred.
- the weight ratio of the expanded graphite to the orientation control particles is preferably 1/4 or more, and more preferably 2/3 or more.
- the weight ratio is preferably 5 or less.
- the expanded graphite can be further oriented in a direction different from the plane direction of the sheet, and the thermal conductivity in the thickness direction can be further increased. Can do.
- Expanded graphite is a laminate of a plurality of graphene layers. Expanded graphite is, for example, graphite having a larger graphene layer than normal graphite such as natural graphite and artificial graphite. In the present specification, expanded graphite includes at least a part of graphene layers expanded from normal graphite.
- the size of the expanded graphite is not particularly limited, but it is preferable to use one having an average particle diameter of 100 ⁇ m to 1000 ⁇ m. In the present specification, the “average particle diameter” is a value measured by a laser diffraction / scattering particle size distribution meter.
- partially exfoliated exfoliated graphite may be used as expanded graphite.
- the partially exfoliated exfoliated graphite is graphite having a portion where an interlayer between graphenes is expanded. More specifically, partially exfoliated exfoliated graphite is graphite in which a portion of the graphene laminate or graphene is partially exfoliated from the edge to some extent by expanding the interlayer between graphenes, and is exfoliated It is.
- Partially exfoliated graphite has a large specific surface area because the interlayer distance between graphenes is increased. Moreover, the partially exfoliated exfoliated graphite is graphite in which the central part has a graphite structure and the edge part is exfoliated. For this reason, it is easier to handle than conventional graphene and exfoliated graphite. Note that exfoliated graphite is a graphene laminate obtained by exfoliating graphite and having a smaller number of graphene layers than the original graphite.
- Partially exfoliated exfoliated graphite includes graphite or primary exfoliated graphite and a resin, and a step of preparing a raw material composition in which the resin is fixed to graphite or primary exfoliated graphite, and is included in the raw material composition It can be obtained by a production method comprising a step of exfoliating graphite or primary exfoliated graphite by thermally decomposing a resin. Although a detailed manufacturing method will be described later, the thermal decomposition of the resin may be performed while a part of the resin remains. Therefore, in the partially exfoliated graphite, a part of the resin fixed to the graphite or primary exfoliated graphite by grafting or adsorption may remain.
- the partially exfoliated exfoliated graphite may include orientation control particles. More specifically, the orientation control particles may be included between the graphene layers in the partially exfoliated exfoliated graphite. In that case, the partially exfoliated exfoliated graphite can be further oriented in a direction different from the sheet surface direction, and the thermal conductivity in the thickness direction can be further increased.
- orientation control particles refer to particles that, by virtue of their presence, can orient at least a portion of expanded graphite in a direction different from the plane direction of the sheet.
- the orientation control particles may be an inorganic compound or an organic compound as long as it has the above function.
- aluminum oxide (Al 2 O 3 ), magnesium oxide (MgO), or the like can be used.
- the average particle diameter of the orientation control particles is not particularly limited, but is preferably 0.2 ⁇ m or more, more preferably 1 ⁇ m or more, further preferably 5 ⁇ m or more, and particularly preferably 10 ⁇ m or more. preferable.
- the average particle size is not less than the above lower limit, the expanded graphite can be further oriented in a direction different from the sheet direction, and the thermal conductivity in the thickness direction can be further increased.
- the average particle diameter of the orientation control particles is preferably 1000 ⁇ m or less, more preferably 500 ⁇ m or less, and further preferably 300 ⁇ m or less.
- the method for producing a heat conductive sheet according to the present invention includes a step of preparing a mixture of expanded graphite and orientation control particles (step 1), and forming the mixture into a sheet, thereby forming at least a part of the expanded graphite into a sheet. And a step of aligning in a direction different from the surface direction (step 2).
- expanded graphite and orientation control particles are mixed to prepare a mixture.
- Mixing of the expanded graphite and the orientation control particles may be performed in a dry state, but is preferably performed in the presence of a supercritical medium.
- a supercritical medium When mixing in a supercritical medium, expanded graphite and orientation control particles can be mixed more uniformly. Therefore, in the sheet forming described later, expanded graphite can be further oriented in a direction different from the surface direction of the sheet, and heat dissipation in the thickness direction of the heat conductive sheet can be further enhanced.
- the supercritical medium for example, water or carbon dioxide (supercritical carbon dioxide) in a supercritical body can be used.
- the expanded graphite and the orientation control particles are uniformly mixed in the mixture obtained in Step 1.
- the orientation control particles are included between the graphene layers of the expanded graphite.
- the sheet forming method using the press is not particularly limited, and for example, it can be produced by the following method. First, the obtained mixture is sandwiched between two metal flat plates, pressed, and allowed to stand for a predetermined time. Thereafter, the obtained sample is heated for a predetermined time and pressed again to form a sheet. The above operation is repeated to produce a plurality of sheets, and the sheets are overlapped and pressed again to obtain a sheet having a predetermined thickness.
- the sheet molding may be performed by filling the mixture into a cylinder and pressing it. Even in the case of using a cylinder, the mixture is first filled in the cylinder, pressed, and allowed to stand for a predetermined time. Thereafter, the obtained sample is heated for a predetermined time and pressed again to form a sheet.
- partially exfoliated exfoliated graphite may be used as expanded graphite in producing a heat conductive sheet. Even in that case, it is preferable that the orientation control particles are included in the partially exfoliated exfoliated graphite from the viewpoint of further orientation of the expanded graphite in a direction different from the plane direction of the sheet.
- a method for producing partially exfoliated exfoliated graphite and a method for including orientation control particles will be described in detail.
- Method for producing partially exfoliated exfoliated graphite In the method of producing partially exfoliated exfoliated graphite, first, a composition in which a resin is fixed to graphite or primary exfoliated graphite is prepared. The resin is fixed to graphite or exfoliated graphite by grafting or adsorption.
- the primary exfoliated graphite includes a large amount of exfoliated graphite obtained by exfoliating graphite. Since primary exfoliated graphite is obtained by exfoliating graphite, the specific surface area may be larger than that of graphite.
- a mixture containing the graphite or primary exfoliated graphite and a radical polymerizable monomer is prepared, and the radical polymerizable monomer is polymerized in the mixture by polymerizing the radical polymerizable monomer in the mixture.
- examples include a method of forming a polymer that is polymerized and grafting the polymer, that is, a resin onto graphite or primary exfoliated graphite.
- radical polymerizable monomer examples include propylene glycol, glycidyl methacrylate, vinyl acetate, butyral, and acrylic acid.
- the polymer radicals generated by pyrolyzing the polymer can be grafted directly to graphite or primary exfoliated graphite. May be.
- the adsorption method it is possible to use a method in which graphite or primary exfoliated graphite and a resin are dissolved or dispersed in an appropriate solvent, and then graphite or primary exfoliated graphite is mixed with the resin in the solvent. .
- ultrasonic treatment is performed in order to effectively adsorb the resin by graphite or primary exfoliated graphite.
- polymers examples include polypropylene glycol, polyglycidyl methacrylate, polyvinyl acetate, polybutyral, and polyacrylic acid.
- the resin in the composition in which the resin is fixed to graphite or primary exfoliated graphite is thermally decomposed by the grafting or adsorption.
- the graphite or the primary exfoliated graphite is peeled off while leaving a part of the resin fixed to the graphite or the primary exfoliated graphite, whereby a partially exfoliated graphite can be obtained.
- the composition may be heated to a temperature higher than the thermal decomposition temperature of the resin.
- the resin is heated above the thermal decomposition temperature of the resin, and the resin is further baked. At this time, it is fired to such an extent that the resin remains in the composition.
- Thermal decomposition so that the resin remains can be achieved by adjusting the heating time. That is, the amount of residual resin can be increased by shortening the heating time. Also, the amount of residual resin can be increased by lowering the heating temperature. In this way, resin-residual partially exfoliated exfoliated graphite can be obtained.
- the thermal decomposition temperature of polyglycidyl methacrylate is about 400 ° C. to 500 ° C.
- the reason why the partially exfoliated exfoliated graphite can be obtained by thermal decomposition of the polymer is considered to be due to the above-described reason. That is, it is considered that when the polymer grafted on the graphite is baked, a large stress acts on the graft point, thereby increasing the distance between the graphenes.
- the grafting step and the thermal decomposition of the polymer may be carried out continuously in the same heating step.
- a composition further including a thermally decomposable foaming agent that generates a gas upon thermal decomposition is prepared.
- the graphite or primary exfoliated graphite can be more effectively exfoliated by heating.
- the thermal decomposable foaming agent is not particularly limited as long as it is a compound that spontaneously decomposes by heating and generates a gas upon decomposition.
- the thermally decomposable foaming agent include foaming agents such as azocarboxylic acid-based, diazoacetamide-based, azonitrile compound-based, benzenesulfohydrazine-based or nitroso compound-based which generate nitrogen gas during decomposition, carbon monoxide during decomposition, A foaming agent that generates carbon dioxide, methane, aldehyde, or the like can be used.
- the above pyrolyzable foaming agents may be used alone or in combination of a plurality of types of foaming agents.
- thermally decomposable foaming agent azodicarbonamide (ADCA) having a structure represented by the following formula (1), or a foaming agent having a structure represented by the following formulas (2) to (4): Can be used.
- ADCA azodicarbonamide
- foaming agents decompose spontaneously by heating, and generate nitrogen gas during decomposition.
- the thermal decomposition temperature of the thermally decomposable foaming agent is not particularly limited, and may be lower or higher than the temperature at which the radical polymerizable monomer spontaneously starts polymerization.
- the thermal decomposition temperature of ADCA having the structure represented by the above formula (1) is 210 ° C.
- the thermal decomposition starting temperature of the foaming agent having the structure represented by the above formulas (2) to (4) is 88 ° C. in this order. 96 ° C and 110 ° C.
- the mixing ratio of the graphite or primary exfoliated graphite and the thermally decomposable foaming agent is not particularly limited, but the pyrolyzable foaming agent is 100 parts by weight to 300 parts by weight with respect to 100 parts by weight of the graphite or primary exfoliated graphite. It is preferable to blend partly.
- the compounding quantity of the said heat decomposable foaming agent into the said range, the said graphite or primary exfoliated graphite can be peeled more effectively, and partial exfoliation type exfoliated graphite can be obtained effectively.
- the thermal decomposition temperature of the orientation control particles is preferably higher than the thermal decomposition temperature of the resin.
- the heating of the raw material composition is preferably performed at a temperature higher than the thermal decomposition temperature of the resin and lower than the thermal decomposition temperature of the orientation control particles. By heating in this range, the orientation control particles can be included in the partially exfoliated exfoliated graphite more efficiently. More specifically, the heating temperature is preferably in the range of about 370 ° C. to 500 ° C.
- GREP-EG average particle diameter 100-2000 ⁇ m
- Al 2 O 3 orientation control particles
- the obtained mixture was filled in a cylinder (size: diameter 25 mm, height 250 mm), pressed at a pressure of 10 to 20 MPa, and pressed for 15 minutes. Thereafter, the mixture was heated at 500 ° C. for 2 hours. After heating, the mixture was pressed again in the cylinder with a pressure of 30-40 MPa applied for 15 minutes. Thereby, a heat conductive sheet was obtained.
- Example 7 Except that the addition amount (weight ratio) of expanded graphite and orientation control particles, the type of orientation control particles or the average particle size of orientation control particles was set as shown in Table 1 below, A heat conductive sheet was obtained.
- GREP-EG Charco Suzuhiro Chemical Co., Ltd., average particle size: 100 to 2000 ⁇ m
- Al 2 O 3 as an orientation control particle
- the obtained mixture was sandwiched between two metal flat plates and pressed at a pressure of 10 to 20 MPa for 15 minutes. Thereafter, the mixture was heated at 500 ° C. for 2 hours. After heating, the mixture was sandwiched again between two metal flat plates, and a pressure of 30 to 40 MPa was applied and pressed for 15 minutes to obtain a sheet. This operation was repeated a plurality of times to obtain a plurality of sheets and laminated them. Thereafter, the laminated sheets were sandwiched between two metal flat plates, and a pressure of 30 to 40 MPa was applied and pressed for 15 minutes to obtain a heat conductive sheet.
- Example 9 Preparation of partially exfoliated exfoliated graphite; Expanded graphite (trade name “PF Powder 8F” manufactured by Toyo Tanso Co., Ltd.) 2.5 g and ADCA (manufactured by Eiwa Kasei Co., Ltd., product name “AC #”) having the structure shown in Formula (1) as a thermally decomposable foaming agent RK ”, thermal decomposition temperature 210 ° C.) 5 g and polyglycidyl methacrylate (manufactured by NOF Corporation, product number“ G2050M ”) 50 g were mixed with tetrahydrafuran 450 g as a solvent to prepare a raw material composition.
- PF Powder 8F manufactured by Toyo Tanso Co., Ltd.
- ADCA manufactured by Eiwa Kasei Co., Ltd., product name “AC #”
- thermal decomposition temperature 210 ° C. thermal decomposition temperature 210 ° C.
- the raw material composition was irradiated with ultrasonic waves at 100 W and an oscillation frequency of 28 kHz for 5 hours using an ultrasonic treatment apparatus (manufactured by Honda Electronics Co., Ltd.).
- Polyglycidyl methacrylate was adsorbed on the expanded graphite by ultrasonic treatment. In this way, a composition in which polyglycidyl methacrylate was adsorbed on expanded graphite was prepared.
- the composition is formed by a solution casting method, maintained at a drying temperature of 80 ° C. for 2 hours, then maintained at 110 ° C. for 1 hour, and further at a temperature of 150 ° C. for 1 hour. And maintained at a temperature of 230 ° C. for 2 hours.
- the ADCA was thermally decomposed and foamed in the composition.
- a heat conductive sheet was obtained in the same manner as in Example 1 except that the obtained partially exfoliated graphite was used as expanded graphite.
- Example 10 A heat conductive sheet was obtained in the same manner as in Example 9 except that the types of orientation control particles were set as shown in Table 1 below.
- FIG. 1 (a) is an SEM photograph at a magnification of 600 times of the cross section of the heat conductive sheet obtained in Example 1.
- FIG. FIG. 1B is an element mapping image of the SEM photograph of FIG.
- FIG. 2A is an SEM photograph with a magnification of 2000 times of the cross section of the heat conductive sheet obtained in Example 1.
- FIG. 2B is an element mapping image of the SEM photograph of FIG.
- FIG. 3A is an SEM photograph with a magnification of 1000 times of the cross section of the heat conductive sheet obtained in Comparative Example 1.
- FIG. FIG. 3B is an element mapping image of the SEM photograph of FIG.
- a white part is Al and a black part is carbon.
- thermo conductivity in the thickness direction Using a product number “LFA447 Nano Flash” manufactured by NETZSCH, the thermal conductivity of a 1 cm square thermal conductive sheet was measured.
- Table 1 below shows the evaluation results of thermal conductivity and specific gravity in the thickness direction in Examples 1 to 11 and Comparative Example 1.
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Abstract
Description
下記の特許文献3には、配向したグラファイト構造体に金属化合物粒子が分散されている高熱伝導性部材が開示されている。
特許文献3の高熱伝導性部材は、グラファイトの配向性を維持しつつ熱伝導性の粒子を混合することにより高熱伝導性を得るものであるが、やはり厚み方向の熱伝導性が十分ではなかった。
本発明に係る熱伝導シートは、好ましくは、前記配向制御粒子の平均粒径が、0.2μm以上、1000μm以下である。
本発明に係る熱伝導シートは、膨張黒鉛と、配向制御粒子とを含む。上記膨張黒鉛の少なくとも一部は、上記配向制御粒子の存在により、シートの面方向とは異なる方向に配向している。そのため、本発明に係る熱伝導シートは、シートの厚み方向における熱伝導性に優れている。もっとも、膨張黒鉛の全てが、シートの面方向とは異なる方向に配向していない場合、本発明に係る熱伝導シートは、シートの面方向における熱伝導性にも優れている。
膨張黒鉛は、複数のグラフェン層の積層体である。膨張黒鉛は、例えば、天然黒鉛や人造黒鉛などの通常の黒鉛よりも、グラフェン層間が大きい黒鉛である。本明細書においては、少なくとも一部のグラフェン層間が通常の黒鉛より拡げられたものも膨張黒鉛に含まれるものとする。膨張黒鉛の大きさとしては、特に限定されないが、平均粒径で、100μm~1000μmのものを用いることが好ましい。なお、本明細書において、「平均粒径」とは、レーザ回折/散乱式粒度分布計により測定された値である。
配向制御粒子とは、その存在により、少なくとも一部の膨張黒鉛を、シートの面方向とは異なる方向に配向させることが可能な粒子のことをいう。配向制御粒子は、上記の機能を有する限り、無機化合物であってもよく、有機化合物であってもよい。
本発明に係る熱伝導シートの製造方法は、膨張黒鉛と、配向制御粒子との混合物を用意する工程(工程1)と、上記混合物をシート成形することによって、上記膨張黒鉛の少なくとも一部をシートの面方向とは異なる方向に配向させる工程(工程2)とを備える。
まず、膨張黒鉛と、配向制御粒子とを混合し、混合物を用意する。膨張黒鉛と、配向制御粒子との混合は、乾燥状態で行ってもよいが、超臨界媒体の存在下で行うことが好ましい。超臨界媒体中で混合する場合、膨張黒鉛と、配向制御粒子とをより一層均一に混合することができる。そのため、後述するシート成形において、膨張黒鉛をシートの面方向とは異なる方向により一層配向させることができ、熱伝導シートの厚み方向の放熱性をより一層高めることができる。なお、超臨界媒体としては、例えば、超臨界状体にある水や二酸化炭素(超臨界二酸化炭素)を用いることができる。
次に、得られた混合物をプレスによりシート成形する。このとき、膨張黒鉛へのプレスは、上記配向制御粒子の存在下で行われる。そのため、上記膨張黒鉛の少なくとも一部がシートの面方向とは異なる方向に配向することとなる。
部分剥離型薄片化黒鉛の製造方法においては、まず樹脂が黒鉛もしくは一次薄片化黒鉛に固定されている組成物を用意する。樹脂の黒鉛もしくは薄片化黒鉛への固定は、グラフト又は吸着により行われる。なお、一次薄片化黒鉛とは、黒鉛を剥離することにより得られた薄片化黒鉛を多く含むものである。一次薄片化黒鉛は、黒鉛を剥離することにより得られるものであるため、その比表面積は、黒鉛よりも大きいものであればよい。
本発明では、上記のようにして用意された、固定化された樹脂の一部が残存している部分剥離型薄片化黒鉛と、配向制御粒子とを含む原料組成物を加熱し、それによって部分剥離型薄片化黒鉛内に配向制御粒子を包摂させることができる。
次に、本発明の具体的な実施例及び比較例を挙げることにより本発明を明らかにする。なお、本発明は以下の実施例に限定されるものではない。
膨張黒鉛(鈴裕化学社製、商品名「GREP-EG」、平均粒径100~2000μm)71.4重量%と、配向制御粒子としてのAl2O3(和光純薬社製、商品名「酸化アルミ」、平均粒径:>75μm)28.6重量%とを、圧力容器に入れ(重量比;膨張黒鉛:配向制御粒子=10:4)、マグネチックスターラーにより、20~100rpmの速度で撹拌した。しかる後、容器内に超臨界二酸化炭素を供給し、容器内の圧力を27.6MPaとして、50℃で6時間撹拌した。撹拌後、超臨界二酸化炭素を抜き取り、膨張黒鉛とAl2O3の混合物を取り出した。
膨張黒鉛及び配向制御粒子の添加量(重量比)、配向制御粒子の種類又は配向制御粒子の平均粒径をそれぞれ下記の表1に示すように設定したこと以外は実施例1と同様にして、熱伝導シートを得た。
膨張黒鉛(炭鈴裕化学社製、商品名「GREP-EG」、平均粒径100~2000μm)50重量%と、配向制御粒子としてのAl2O3(和光純薬社製、商品名「酸化アルミ」、平均粒径0.236μm)50重量%とを、圧力容器に入れ(重量比;膨張黒鉛:配向制御粒子=10:10)、マグネチックスターラーにより、20~100rpmの速度で撹拌した。しかる後、容器内に超臨界二酸化炭素を供給し、容器内の圧力を27.6MPaとして、50℃で6時間撹拌した。撹拌後、超臨界二酸化炭素を抜き取り、膨張黒鉛とAl2O3の混合物を取り出した。
部分剥離型薄片化黒鉛の調製;
膨張黒鉛(東洋炭素社製、商品名「PFパウダー8F」)2.5gと、熱分解性発泡剤として、式(1)に示した構造を有するADCA(永和化成社製、商品名「AC♯R-K」、熱分解温度210℃)5gと、ポリグリシジルメタクリレート(日本油脂社製、品番「G2050M」)50gとを、溶媒としてのテトラヒドラフラン450gと混合し、原料組成物を用意した。原料組成物に、超音波処理装置(本多電子社製)を用い、100W、発振周波数28kHzで5時間超音波を照射した。超音波処理により、ポリグリシジルメタクリレートを膨張黒鉛に吸着させた。このようにして、ポリグリシジルメタクリレートが膨張黒鉛に吸着されている組成物を用意した。
配向制御粒子の種類を下記の表1に示すように設定したこと以外は実施例9と同様にして、熱伝導シートを得た。
実施例9と同様の方法で作製した部分剥離型薄片化黒鉛71.4重量%と、配向制御粒子としてのMgO(和光純薬社製、商品名「酸化マグネシウム」、平均粒径40~70μm))28.6重量%とを、圧力容器に入れ(重量比;膨張黒鉛:配向制御粒子=10:4)、マグネチックスターラーにより、20~100rpmの速度で撹拌した。室温で6時間撹拌した後、膨張黒鉛とMgOの混合物を取り出した。その他の点は、実施例1と同様にして、熱伝導シートを得た。
膨張黒鉛(東洋炭素社製、商品名「PFパウダー8F」、平均粒径10~300μm)100重量%を、シリンダー(大きさ:直径25mm、高さ250mm)内に充填し、10~20MPaの圧力を加えて、15分間プレスした。しかる後、混合物を500℃で2時間加熱した。加熱後、混合物を再度シリンダー内で、30~40MPaの圧力を加えて、15分間プレスした。それによって、熱伝導シートを得た。
(SEM写真による断面観察)
熱伝導シートを、ダイヤモンドワイヤーソーにより切り出し、その断面を走査型電子顕微鏡(日立ハイテクノロジーズ社製、型番「S-3400N」)を用いて観察した。また、EDX(日立ハイテクノロジーズ社製、型番「S-3400N」)を用いて、得られた走査型電子顕微鏡写真(SEM写真)の元素マッピング像を得た。
NETZSCH社製、品番「LFA447 ナノフラッシュ」を使用して、1cm角の熱伝導シートの熱伝導率を測定した。
熱伝導測定を行う1cm角の熱伝導シートの厚み(d)cmと重量(W)gを測定した。比重は、W/(1×1×d)により算出した。
Claims (12)
- 熱伝導シートであって、
膨張黒鉛と、配向制御粒子とを含み、
前記膨張黒鉛の少なくとも一部が、前記配向制御粒子の存在により、シートの面方向とは異なる方向に配向している、熱伝導シート。 - 前記膨張黒鉛の少なくとも一部が、前記配向制御粒子の存在により、シートの厚み方向に配向している、請求項1に記載の熱伝導シート。
- 厚み方向の熱伝導率が、5W/m・K以上である、請求項1又は2に記載の熱伝導シート。
- 前記膨張黒鉛の前記配向制御粒子に対する重量比(膨張黒鉛/配向制御粒子)が、1/4以上、5以下の範囲にある、請求項1~3のいずれか1項に記載の熱伝導シート。
- 比重が、1.5g/cm3以上、5g/cm3以下の範囲内にある、請求項1~4のいずれか1項に記載の熱伝導シート。
- 前記膨張黒鉛が、部分的にグラフェンが剥離している構造を有する部分剥離型薄片化黒鉛である、請求項1~5のいずれか1項に記載の熱伝導シート。
- 前記部分剥離型薄片化黒鉛内に、前記配向制御粒子が包摂されている、請求項6に記載の熱伝導シート。
- 前記配向制御粒子が、無機化合物である、請求項1~7のいずれか1項に記載の熱伝導シート。
- 前記配向制御粒子の平均粒径が、0.2μm以上、1000μm以下である、請求項1~8のいずれか1項に記載の熱伝導シート。
- 熱伝導シートの製造方法であって、
膨張黒鉛と、配向制御粒子との混合物を用意する工程と、
前記混合物をプレスによりシート成形することによって、前記膨張黒鉛の少なくとも一部をシートの面方向とは異なる方向に配向させる工程とを備える、熱伝導シートの製造方法。 - 前記混合物を用意する工程において、前記膨張黒鉛と、前記配向制御粒子とを、超臨界媒体の存在下で混合する、請求項10に記載の熱伝導シートの製造方法。
- 前記シート成形が、前記混合物をシリンダー内に充填して、プレスすることにより行われる、請求項10又は11に記載の熱伝導シートの製造方法。
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JP2018026527A (ja) * | 2016-07-28 | 2018-02-15 | ジャパンマテックス株式会社 | 混合グラファイトを用いた放熱材およびその製造方法 |
WO2019117064A1 (ja) | 2017-12-12 | 2019-06-20 | 積水化学工業株式会社 | 熱伝導シート |
WO2020027041A1 (ja) * | 2018-07-30 | 2020-02-06 | 株式会社Adeka | 複合材料の製造方法 |
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JP6200593B2 (ja) | 2015-05-14 | 2017-09-20 | 積水化学工業株式会社 | 炭素質材料、炭素質材料−活物質複合体、リチウムイオン二次電池用電極材及びリチウムイオン二次電池 |
CN113307258A (zh) * | 2021-05-28 | 2021-08-27 | 黑龙江益墨轩新材料科技有限公司 | 一种石墨烯电热板的制备方法 |
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- 2015-11-27 EP EP15864565.5A patent/EP3228590A4/en active Pending
- 2015-11-27 JP JP2016562425A patent/JP6650412B2/ja active Active
- 2015-11-27 CN CN201580043141.4A patent/CN106573779B/zh active Active
- 2015-11-27 US US15/508,740 patent/US20170298261A1/en not_active Abandoned
- 2015-11-27 KR KR1020167035782A patent/KR20170091508A/ko unknown
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Cited By (6)
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JP2018026527A (ja) * | 2016-07-28 | 2018-02-15 | ジャパンマテックス株式会社 | 混合グラファイトを用いた放熱材およびその製造方法 |
WO2019117064A1 (ja) | 2017-12-12 | 2019-06-20 | 積水化学工業株式会社 | 熱伝導シート |
KR20200091807A (ko) | 2017-12-12 | 2020-07-31 | 세키스이가가쿠 고교가부시키가이샤 | 열전도 시트 |
WO2020027041A1 (ja) * | 2018-07-30 | 2020-02-06 | 株式会社Adeka | 複合材料の製造方法 |
JPWO2020027041A1 (ja) * | 2018-07-30 | 2021-08-02 | 株式会社Adeka | 複合材料の製造方法 |
JP7407711B2 (ja) | 2018-07-30 | 2024-01-04 | 株式会社Adeka | 複合材料の製造方法 |
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JPWO2016088682A1 (ja) | 2017-09-07 |
CN106573779B (zh) | 2021-06-18 |
EP3228590A4 (en) | 2018-07-25 |
JP6650412B2 (ja) | 2020-02-19 |
CN106573779A (zh) | 2017-04-19 |
EP3228590A1 (en) | 2017-10-11 |
TW201632607A (zh) | 2016-09-16 |
KR20170091508A (ko) | 2017-08-09 |
TWI689579B (zh) | 2020-04-01 |
US20170298261A1 (en) | 2017-10-19 |
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