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WO2024204485A1 - Spherical magnesium oxide, production method for same, thermally conductive filler, and resin composition - Google Patents

Spherical magnesium oxide, production method for same, thermally conductive filler, and resin composition Download PDF

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Publication number
WO2024204485A1
WO2024204485A1 PCT/JP2024/012542 JP2024012542W WO2024204485A1 WO 2024204485 A1 WO2024204485 A1 WO 2024204485A1 JP 2024012542 W JP2024012542 W JP 2024012542W WO 2024204485 A1 WO2024204485 A1 WO 2024204485A1
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Prior art keywords
magnesium oxide
spherical magnesium
spherical
titanium
iron
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French (fr)
Japanese (ja)
Inventor
彰範 齋藤
善久 大崎
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Tateho Chemical Industries Co Ltd
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Tateho Chemical Industries Co Ltd
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    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01FCOMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
    • C01F5/00Compounds of magnesium
    • C01F5/02Magnesia
    • C01F5/06Magnesia by thermal decomposition of magnesium compounds
    • C01F5/08Magnesia by thermal decomposition of magnesium compounds by calcining magnesium hydroxide
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01GCOMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
    • C01G49/00Compounds of iron
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/18Oxygen-containing compounds, e.g. metal carbonyls
    • C08K3/20Oxides; Hydroxides
    • C08K3/22Oxides; Hydroxides of metals
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K7/00Use of ingredients characterised by shape
    • C08K7/16Solid spheres
    • C08K7/18Solid spheres inorganic
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L101/00Compositions of unspecified macromolecular compounds

Definitions

  • the present invention relates to spherical magnesium oxide and a method for producing the same, as well as a thermally conductive filler containing the spherical magnesium oxide and a resin composition containing the same.
  • Silica, alumina, etc. have traditionally been used as thermally conductive fillers, but silica has low thermal conductivity and is insufficient at dissipating heat to cope with the increase in heat generated by recent trends such as high integration, high power consumption, and high speed, which can cause problems with the stable operation of semiconductors.
  • alumina has a higher thermal conductivity than silica, and improves heat dissipation compared to silica, but alumina's high hardness causes severe wear on kneading machines, molding machines, molds, etc., which is a problem.
  • magnesium oxide which has a thermal conductivity one order of magnitude higher than silica and about twice that of alumina, and is also less hard than alumina, and can suppress wear on each manufacturing equipment, is being considered as a thermally conductive filler.
  • Patent Document 1 proposes magnesium oxide in which a boron compound or the like is added to control the aggregation state and particle size distribution.
  • Patent Document 2 proposes spherical magnesium oxide with a smooth and dense surface, which is obtained by adding a lithium compound.
  • Patent Document 3 proposes spherical magnesium oxide with excellent moisture resistance and filling properties, which is obtained by adjusting the boron and iron content within a certain range.
  • the objective of the present invention is to provide spherical magnesium oxide that has high sphericity, excellent filling ability into resin, and small increase in viscosity when kneaded into resin, and a method for producing the same.
  • the gist of the present invention is as follows.
  • D 50 volume-based cumulative 50% particle size
  • the spherical magnesium oxide of [1] having a cumulative 50% particle diameter (D 50 ) of more than 25 ⁇ m and not more than 150 ⁇ m.
  • a method for producing spherical magnesium oxide comprising the steps of: 1) reacting an aqueous magnesium chloride solution with an aqueous alkali solution to prepare a magnesium hydroxide slurry; 2) drying and calcining the magnesium hydroxide slurry to prepare magnesium oxide; 3) dispersing the magnesium oxide in a solvent to prepare a dispersion, followed by wet-grinding; 4) spray-drying the magnesium oxide dispersion after wet-grinding; and 5) calcining the spherical magnesium oxide granulated by spray-drying, wherein in at least one of steps 1) to 5), the titanium and/or iron content is adjusted so that the spherical magnesium oxide after calcination has a titanium content of 0.05 to 2.0% and an iron content of 100 to 1,500 ppm.
  • the present invention provides spherical magnesium oxide with high sphericity, excellent fillability into resin, and small increase in viscosity when filled into resin, as well as a method for producing the same.
  • the spherical magnesium oxide of the present invention contains 0.05 to 2.0% titanium and 100 to 1,500 ppm iron, has a volume-based cumulative 50% particle size (D 50 ) in the range of 3 to 200 ⁇ m as measured by laser diffraction scattering particle size distribution measurement, and has a sphericity of 1.00 to 1.20 as read from a SEM photograph.
  • D 50 volume-based cumulative 50% particle size
  • % means % by mass
  • ppm means ppm by mass, unless otherwise specified.
  • the spherical magnesium oxide of the present invention is intended to be magnesium oxide powder.
  • the spherical magnesium oxide obtained in the present invention has a volume-based cumulative 50% particle size ( D50 ) measured by laser diffraction/scattering particle size distribution measurement of 3 to 200 ⁇ m, preferably 15 to 180 ⁇ m, and more preferably more than 25 ⁇ m and not more than 150 ⁇ m, which is a relatively large particle size range capable of improving heat dissipation performance, and also has high sphericity and excellent filling ability.
  • D50 volume-based cumulative 50% particle size measured by laser diffraction/scattering particle size distribution measurement of 3 to 200 ⁇ m, preferably 15 to 180 ⁇ m, and more preferably more than 25 ⁇ m and not more than 150 ⁇ m, which is a relatively large particle size range capable of improving heat dissipation performance, and also has high sphericity and excellent filling ability.
  • sphericity refers to the sphericity that can be read from a scanning electron microscope (SEM) photograph, and should be 1.00 to 1.20, preferably 1.00 to 1.15, and more preferably 1.00 to 1.10. Such sphericity provides excellent filling properties into resin.
  • SEM scanning electron microscope
  • the lengths of the major and minor axes passing through the center of the particles are measured for 100 particles in an electron microscope photograph taken using an SEM, the ratio of the major axis to the minor axis is calculated, and the average value is taken as the sphericity.
  • the titanium content is 0.05 to 2.0%, preferably 0.08 to 1.5%, and more preferably 0.1 to 1.0%.
  • the iron content is 100 to 1,500 ppm, preferably 150 to 1,300 ppm, and more preferably 200 to 1,000 ppm.
  • the method for producing spherical magnesium oxide of the present invention is not particularly limited, but can be produced, for example, by the following production method: 1) a step of reacting an aqueous magnesium chloride solution with an aqueous alkali solution to prepare magnesium hydroxide slurry, 2) a step of drying and firing the magnesium hydroxide slurry to prepare magnesium oxide, 3) a step of dispersing the magnesium oxide in a solvent to prepare a dispersion liquid, which is then wet-pulverized, 4) a step of spray-drying the magnesium oxide dispersion liquid after wet-pulverization, and 5) a step of firing the spherical magnesium oxide granulated by spray drying, and in at least one or more of the steps 1) to 5), the titanium and/or iron content is adjusted so that the titanium content in the spherical magnesium oxide after firing is 0.05 to 2.0% and the iron content is 100 to 1,500 ppm.
  • the above-mentioned production method can be carried out as follows. 1) A magnesium chloride aqueous solution is reacted with an alkaline aqueous solution to obtain a magnesium hydroxide slurry, and then 2) The slurry is filtered, washed with water, dried, and then calcined to obtain magnesium oxide. 3) The magnesium oxide is dispersed in a solvent, preferably an organic solvent, to obtain a dispersion liquid, which is then wet-pulverized. 4) Spray drying is carried out; 5) The obtained spherical magnesium oxide is fired to obtain the desired spherical magnesium oxide.
  • a titanium source and/or an iron source are mixed and/or added before the final firing so that the titanium content of the spherical magnesium oxide after the final firing is 0.05 to 2.0% and the iron content is 100 to 1,500 ppm.
  • the titanium content and/or the iron source are adjusted by, for example, a) adding a boron source and/or an iron source to an aqueous magnesium chloride solution and/or an alkaline aqueous solution, b) adding a titanium source and/or an iron source to the generated magnesium hydroxide slurry, c) mixing a titanium source and/or an iron source with magnesium oxide obtained by firing magnesium hydroxide, d) adding a titanium source and/or an iron source during wet grinding of magnesium oxide, e) mixing a titanium source and/or an iron source with spherical magnesium oxide granulated by spray drying, or the like, to adjust the titanium content and iron content in the spherical magnesium oxide finally obtained.
  • the titanium content and the iron content may be adjusted
  • the titanium source is not particularly limited as long as it is a compound containing titanium, but examples include titanium oxide (anatase type, rutile type), titanium chloride, titanium hydroxide, titanium bromide, titanium fluoride, magnesium titanate, etc.
  • the iron source is not particularly limited as long as it is a compound containing iron, but examples include iron oxide (II), iron oxide (III), iron tetroxide, iron hydroxide, iron chloride, iron nitride, iron bromide, and iron fluoride.
  • the titanium source is adjusted so that the titanium content of the spherical magnesium oxide after final firing is 0.05-2.0%. If the titanium content is less than 0.05%, the effect of reducing viscosity is not sufficient. Furthermore, if the titanium content exceeds 2.0%, excessive particle growth and adhesion between particles are likely to occur, making it impossible to obtain spherical magnesium oxide with high sphericity. Then, the iron source is adjusted so that the iron content of the spherical magnesium oxide after final firing is 100-1,500 ppm. In addition to the above titanium content, if the iron content is in the range of 100-1,500 ppm, spherical magnesium oxide with high sphericity tends to be obtained.
  • the magnesium chloride aqueous solution can be selected from, for example, magnesium chloride hexahydrate, magnesium chloride dihydrate, anhydrous magnesium chloride, bittern, seawater, and combinations thereof.
  • the alkaline aqueous solution can be selected from, for example, an aqueous sodium hydroxide solution, an aqueous calcium hydroxide solution, ammonia water, and combinations thereof.
  • the magnesium hydroxide slurry obtained by reacting an aqueous magnesium chloride solution with an aqueous alkali solution is filtered, washed with water, dried, and then calcined to form magnesium oxide, for example, by a method common in the technical field.
  • the obtained magnesium oxide is then dispersed in a solvent to form a dispersion (for example, a slurry), which is wet-pulverized and spray-dried to form granules.
  • the solvent used here is not particularly limited, but any known solvent can be used, such as water-based systems, water-organic solvent mixtures, alcohols such as methanol and ethanol, ketones such as acetone, esters such as ethyl acetate, ethers such as diethyl ether, and aromatic compound solvents such as tetrahydrofuran and toluene.
  • the method of spray drying is not particularly limited, but it is preferable to use a spray drying method in which a magnesium oxide dispersion (e.g., a slurry) after wet grinding is sprayed from a rotating disk or nozzle to obtain magnesium oxide particles.
  • a magnesium oxide dispersion e.g., a slurry
  • the operating conditions are appropriately adjusted according to the slurry viscosity, the particle size of the powder in the slurry, the target particle size, and the like.
  • a dispersant may be appropriately added to the slurry.
  • the operating conditions are not particularly limited, but in the case of the spray drying method, for example, a slurry with a viscosity adjusted to 10 to 3000 cps is sprayed from a rotating disk or nozzle into an air flow at 80°C to 250°C by appropriately adjusting the flow rate, and particles of about 1 to 200 ⁇ m can be produced.
  • the spray conditions by appropriately setting the spray conditions, the sphericity of the obtained spherical magnesium oxide can be adjusted.
  • the cumulative 50% particle size (D 50 ) of the obtained spherical magnesium oxide can be adjusted.
  • the spray drying method is preferred since it can stably obtain particles having a large particle size.
  • the conditions for sintering the granulated magnesium oxide are not particularly limited as long as they are within the range in which the magnesium oxide particles are sintered, but a temperature of 1000°C to 1800°C is preferable, 1100°C to 1700°C is more preferable, and 1200°C to 1600°C is particularly preferable.
  • the sintering time depends on the sintering temperature, but is preferably 0.5 to 10 hours. If the sintering temperature is less than 1000°C, sufficient sintering will not occur, and if it exceeds 1800°C, the particles will sinter together and form coarse agglomerates, so it is adjusted to the above range.
  • the spherical magnesium oxide of the present invention can also be surface-treated using a known method for the purpose of improving moisture resistance.
  • a known method for the purpose of improving moisture resistance there are no particular limitations on the surface treatment agent used, but examples that can be used include colloidal silica, silane-based coupling agents, titania sol, titanate-based coupling agents, phosphorus compounds, alumina sol, aluminate-based coupling agents, zirconium-based coupling agents, etc. These may be used alone or in combination of two or more types.
  • silane coupling agents examples include vinyltrichlorosilane, vinyltrialkoxysilane, glycidoxypropyltrialkoxysilane, and methacryloxypropylmethyldialkoxysilane.
  • Titanate coupling agents include, for example, tetraisopropyl titanate, tetranormalbutyl titanate, tetraoctyl titanate, tetrastearyl titanate, isopropyltriisostearoyl titanate, tetraoctylbis(ditridecylphosphite)titanate, bis(dioctylpyrophosphate)oxyacetate titanate, etc.
  • the phosphorus compound is not particularly limited as long as it is a compound that can react with magnesium oxide to form a magnesium phosphate compound, but examples include phosphoric acid, phosphates, and acidic phosphate esters.
  • acidic phosphate esters include isopropyl acid phosphate, 2-ethylhexyl acid phosphate, oleyl acid phosphate, methyl acid phosphate, ethyl acid phosphate, propyl acid phosphate, butyl acid phosphate, lauryl acid phosphate, and stearyl acid phosphate.
  • aluminate coupling agents include aluminum isopropylate, monosec-butoxyaluminum diisopropylate, aluminum sec-butylate, aluminum ethyl acetoacetate diisopropylate, aluminum tris(ethyl acetoacetate), and aluminum alkyl acetoacetate diisopropylate.
  • zirconium-based coupling agents examples include normal propyl zirconate and normal butyl zirconate.
  • the spherical magnesium oxide of the present invention has the advantages of high sphericity, excellent filling properties, and small increase in viscosity when filled into resin, and can therefore be suitably blended into resin as a filler, making it useful as a thermally conductive filler.
  • the thermally conductive filler of the present invention may contain the spherical magnesium oxide of the present invention alone, or may contain the spherical magnesium oxide of the present invention together with other thermally conductive filler materials.
  • the resin composition of the present invention contains the thermally conductive filler of the present invention, and examples of resins that can be used in the present invention include thermosetting resins and thermoplastic resins.
  • Thermosetting resins are not particularly limited, but examples include phenolic resins, urea resins, melamine resins, alkyd resins, polyester resins, epoxy resins, diallyl phthalate resins, polyurethane resins, and silicone resins.
  • Thermoplastic resins are not particularly limited, but examples include polyamide resins, polyacetal resins, polycarbonate resins, polybutylene terephthalate resins, polyolefin resins, polysulfone resins, polyamideimide resins, polyetherimide resins, polyarylate resins, polyphenylene sulfide resins, polyether ether ketone resins, fluororesins, and liquid crystal polymers.
  • the amount of spherical magnesium oxide in the resin composition of the present invention may be appropriately determined depending on the properties required of the resin composition, and is not particularly limited. However, as an example, spherical magnesium oxide may be used in the range of 0.1 to 100 parts by mass per 100 parts by mass of resin.
  • the resin composition containing the spherical magnesium oxide of the present invention can be used in various fields depending on the characteristics of the resin. However, since the spherical magnesium oxide of the present invention has excellent thermal conductivity, it can be used particularly preferably in applications where heat dissipation is required. For example, the resin composition of the present invention can be used as a semiconductor encapsulation material with excellent thermal conductivity.
  • Measurement and evaluation methods (1) Measurement method of iron content The iron content was measured by ICP emission spectrometry. The measurement sample was added to 12N hydrochloric acid (special grade reagent) and heated to completely dissolve, and the iron content was measured using an ICP measurement device (PS3520 VDD, manufactured by Hitachi High-Tech Science Corporation).
  • the titanium content was measured using an X-ray fluorescence analyzer (device name: ZSX Primus4, manufactured by Rigaku Corporation).
  • the magnesium oxide to be measured was placed in an aluminum ring ( ⁇ 35 mm), sandwiched between dies, and pelletized using a press (surface pressure 250 MPa) to obtain a measurement sample.
  • This sample was measured in SQX analysis (EZ scan) mode (bulb: Rh (4 kW), atmosphere: vacuum, analysis window: Be (30 ⁇ m), measurement diameter: 30 mm ⁇ , measurement range F to U) to determine the titanium content in the magnesium oxide.
  • volume-based cumulative 50% particle size ( D50 ) 0.1 ⁇ 10 ⁇ 3 kg of the measurement sample was precisely weighed, dispersed in 40 mL of methanol, and measured using a laser diffraction scattering type particle size distribution measuring device (MT3300, manufactured by Nikkiso Co., Ltd.).
  • Viscosity evaluation during resin filling Spherical magnesium oxide to be evaluated and alumina particles were mixed at 50% by volume, and this was added to silicone oil (Shin-Etsu Chemical's "KF96-100cs") so that the total filling rate of the spherical magnesium oxide and alumina particles was 75% by volume. This was mixed for 30 seconds at a rotation speed of 2,200 rpm using a rotation/revolution mixer, and then vacuum degassed to obtain a resin composition.
  • the viscosity of the obtained resin composition was measured using a B-type viscometer (TOKIMEC's BL type, measurement conditions: sample temperature 25°C, 6 rpm, rotor No. 4, container dimensions ⁇ 26 mm ⁇ h46 mm, sample amount 20 mL).
  • Example 1 Anhydrous magnesium chloride (MgCl 2 ) was dissolved in ion-exchanged water to prepare an aqueous magnesium chloride solution of about 3.5 mol/l.
  • the MgCl 2 solution and 25% NaOH solution were each pumped into a reactor with a metering pump so that the reaction rate of MgCl 2 was 90 mol%, and a continuous reaction was carried out to obtain a magnesium hydroxide slurry.
  • titanium oxide/anatase type manufactured by Teika Co., Ltd., JA-20
  • titanium oxide/anatase type manufactured by Teika Co., Ltd., JA-20
  • iron oxide (II) manufactured by Hayashi Pure Chemical Industries Co., Ltd.
  • the obtained magnesium hydroxide was fired at 900°C for 1 hour to obtain magnesium oxide.
  • the obtained magnesium oxide was dispersed in an organic solvent to obtain a slurry with a magnesium oxide concentration of 65 wt%.
  • Example 2 Spherical magnesium oxide was obtained using the same production method as in Example 1, except that titanium oxide was added to the reaction liquid so that the titanium content in the spherical magnesium oxide was 0.39% and iron (II) oxide was added to the reaction liquid so that the iron content was 330 ppm.
  • Example 3 Spherical magnesium oxide was obtained using the same production method as in Example 1, except that titanium oxide was added to the reaction liquid so that the titanium content in the spherical magnesium oxide was 0.11% and iron (II) oxide was added to the reaction liquid so that the iron content was 330 ppm.
  • Example 4 Spherical magnesium oxide was obtained using the same manufacturing method as in Example 1, except that titanium oxide was added to the reaction solution so that the titanium content in the spherical magnesium oxide was 0.75% and iron (II) oxide was added so that the iron content was 240 ppm, and the firing temperature in the final firing was 1300°C.
  • the spherical magnesium oxide of Examples 1 to 4 had high sphericity and the increase in viscosity when filled with resin was kept low.
  • the spherical magnesium oxide of Comparative Example 1 had high sphericity, but the increase in viscosity when filled with resin was large, and its performance as a filler was poor.
  • the spherical magnesium oxide of the present invention has a small increase in viscosity when filled into resin, has high sphericity, and is excellent in fillability into resin. Therefore, it was found that the spherical magnesium oxide of the present invention is useful as an excellent resin filler.
  • the present invention provides spherical magnesium oxide that exhibits a small increase in viscosity when filled into resin, has high sphericity, and is excellent in fillability into resin, as well as a method for producing the same.

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Abstract

The purpose of the present invention is to provide: spherical magnesium oxide that high sphericity and excellent filling properties with respect to resin, and that exhibits little increase in viscosity when kneaded with resin; and a production method for the same. The present invention is spherical magnesium oxide comprising 0.05-2.0% titanium and 100-1,500 ppm iron, wherein volume-based cumulative 50% particle diameter (D50) as found by laser diffraction particle size distribution measurement is in the range of 3-200 μm, and sphericity as observed from an SEM image is 1.00-1.20.

Description

球状酸化マグネシウム、その製造方法、熱伝導性フィラー及び樹脂組成物Spherical magnesium oxide, its manufacturing method, thermally conductive filler, and resin composition

 本発明は、球状酸化マグネシウム及びその製造方法並びに前記球状酸化マグネシウムを含有する熱伝導性フィラー及びそれを含有する樹脂組成物に関する。 The present invention relates to spherical magnesium oxide and a method for producing the same, as well as a thermally conductive filler containing the spherical magnesium oxide and a resin composition containing the same.

 熱伝導性フィラーとしては、従来からシリカ、アルミナ等が使用されているが、シリカは、熱伝導率が低く、近年の高集積化、高電力化、高速化等による発熱量の増大に対応する放熱が充分ではなく、半導体の安定動作等に問題が生じる可能性がある。一方、シリカより熱伝導率が高いアルミナは、シリカに比べ放熱性は改善されるが、アルミナは硬度が高いために、混練機、成型機、金型等の摩耗が激しくなるという問題点がある。そこで、熱伝導率がシリカに比べて1桁高く、アルミナに比べて約2倍であり、かつ硬度がアルミナに比べて低く、各製造設備の磨耗を抑制できる酸化マグネシウムが熱伝導性フィラーとして検討されている。 Silica, alumina, etc. have traditionally been used as thermally conductive fillers, but silica has low thermal conductivity and is insufficient at dissipating heat to cope with the increase in heat generated by recent trends such as high integration, high power consumption, and high speed, which can cause problems with the stable operation of semiconductors. On the other hand, alumina has a higher thermal conductivity than silica, and improves heat dissipation compared to silica, but alumina's high hardness causes severe wear on kneading machines, molding machines, molds, etc., which is a problem. For this reason, magnesium oxide, which has a thermal conductivity one order of magnitude higher than silica and about twice that of alumina, and is also less hard than alumina, and can suppress wear on each manufacturing equipment, is being considered as a thermally conductive filler.

 そして、より熱伝導性フィラーに適した酸化マグネシウムを得るために、これまでにも種々の技術開発がなされてきた。特許文献1ではホウ素化合物等を添加し、凝集状態や粒度分布をコントロールした酸化マグネシウムが提案されている。特許文献2では、リチウム化合物を添加することによって得られる、表面が平滑で緻密な球状酸化マグネシウムが提案されている。特許文献3には、ホウ素と鉄の含有量を一定の範囲に調整することによって得られる、耐湿性及び充填性に優れる球状酸化マグネシウムが提案されている。 Various technological developments have been made to obtain magnesium oxide that is more suitable as a thermally conductive filler. Patent Document 1 proposes magnesium oxide in which a boron compound or the like is added to control the aggregation state and particle size distribution. Patent Document 2 proposes spherical magnesium oxide with a smooth and dense surface, which is obtained by adding a lithium compound. Patent Document 3 proposes spherical magnesium oxide with excellent moisture resistance and filling properties, which is obtained by adjusting the boron and iron content within a certain range.

特開2011-020870号公報JP 2011-020870 A 特開2016-088838号公報JP 2016-088838 A 特開2018-131378号公報JP 2018-131378 A

 特許文献1~3のように、従来、熱伝導性フィラーとしての酸化マグネシウムは、充填性の向上を主な技術開発の目的としてきた。一方で、樹脂加工を容易とするような、フィラーを樹脂に充填した際の粘度上昇の改善も期待されていたが、これまでに、この観点からの技術開発は十分になされていなかった。そこで、本発明は、真球度が高く樹脂への充填性に優れ、かつ樹脂に混錬した際の粘度上昇が小さい球状酸化マグネシウム及びその製造方法を提供することを課題とする。 As shown in Patent Documents 1 to 3, conventionally, the main objective of technological development for magnesium oxide as a thermally conductive filler has been to improve the filling ability. On the other hand, there has also been hope for an improvement in the increase in viscosity that occurs when the filler is filled into a resin, to facilitate resin processing, but technological development from this perspective has not been sufficient to date. Therefore, the objective of the present invention is to provide spherical magnesium oxide that has high sphericity, excellent filling ability into resin, and small increase in viscosity when kneaded into resin, and a method for producing the same.

 上記の課題を解決するために、本発明者は、種々検討を重ねた結果、チタン及び鉄の含有量を一定の範囲に調整することで、真球度が高く樹脂への充填性に優れ、かつ樹脂充填時の粘度上昇が小さい球状酸化マグネシウムが得られることを見出して、本発明を完成させた。そこで、本発明の要旨は以下のとおりである。 In order to solve the above problems, the inventors conducted extensive research and discovered that by adjusting the titanium and iron content within a certain range, it is possible to obtain spherical magnesium oxide that has high sphericity, excellent fillability into resin, and small increase in viscosity when filled into resin, and thus completed the present invention. The gist of the present invention is as follows.

[1] チタン0.05~2.0%及び鉄100~1,500ppmを含有し、レーザー回折散乱式粒度分布測定による体積基準の累積50%粒子径(D50)が3~200μmの範囲であり、SEM写真から読み取れる真球度が1.00~1.20である、球状酸化マグネシウム。 [1] Spherical magnesium oxide containing 0.05 to 2.0% titanium and 100 to 1,500 ppm iron, having a volume-based cumulative 50% particle size (D 50 ) in the range of 3 to 200 μm as measured by laser diffraction/scattering particle size distribution measurement, and having a sphericity of 1.00 to 1.20 as measured by SEM photography.

[2] 累積50%粒子径(D50)が、25μmより大きく150μm以下である、[1]の球状酸化マグネシウム。 [2] The spherical magnesium oxide of [1], having a cumulative 50% particle diameter (D 50 ) of more than 25 μm and not more than 150 μm.

[3] [1]又は[2]の球状酸化マグネシウムを含有する熱伝導性フィラー。 [3] A thermally conductive filler containing spherical magnesium oxide of [1] or [2].

[4] [3]の熱伝導性フィラーを含有する樹脂組成物。 [4] A resin composition containing the thermally conductive filler of [3].

[5] 1)塩化マグネシウム水溶液とアルカリ水溶液とを反応させて水酸化マグネシウムスラリーを準備する工程と、2)前記水酸化マグネシウムスラリーを乾燥及び焼成して、酸化マグネシウムを準備する工程と、3)前記酸化マグネシウムを溶媒に分散させ分散液とし、その後湿式粉砕する工程と、4)湿式粉砕後の酸化マグネシウム分散液を噴霧乾燥する工程と、5)噴霧乾燥により造粒した球状酸化マグネシウムを焼成する工程と、を含み、前記1)~5)の少なくとも1つ以上の工程において、焼成後の球状酸化マグネシウムにおけるチタン含有量が0.05~2.0%に、及び鉄含有量が100~1,500ppmになるように、チタン及び/又は鉄の含有量を調整する、球状酸化マグネシウムの製造方法。 [5] A method for producing spherical magnesium oxide, comprising the steps of: 1) reacting an aqueous magnesium chloride solution with an aqueous alkali solution to prepare a magnesium hydroxide slurry; 2) drying and calcining the magnesium hydroxide slurry to prepare magnesium oxide; 3) dispersing the magnesium oxide in a solvent to prepare a dispersion, followed by wet-grinding; 4) spray-drying the magnesium oxide dispersion after wet-grinding; and 5) calcining the spherical magnesium oxide granulated by spray-drying, wherein in at least one of steps 1) to 5), the titanium and/or iron content is adjusted so that the spherical magnesium oxide after calcination has a titanium content of 0.05 to 2.0% and an iron content of 100 to 1,500 ppm.

 なお、前記[1]から[5]の各構成は、任意に2つ以上を選択して組み合わせることができる。 Note that any two or more of the configurations [1] to [5] above can be selected and combined.

 本発明によれば、真球度が高く樹脂への充填性に優れ、かつ樹脂充填時の粘度上昇が小さい球状酸化マグネシウム及びその製造方法を提供することができる。 The present invention provides spherical magnesium oxide with high sphericity, excellent fillability into resin, and small increase in viscosity when filled into resin, as well as a method for producing the same.

 本発明の球状酸化マグネシウムは、チタン0.05~2.0%及び鉄100~1,500ppmを含有し、レーザー回折散乱式粒度分布測定による体積基準の累積50%粒子径(D50)が3~200μmの範囲であり、SEM写真から読み取れる真球度が1.00~1.20である。なお、明細書中、含有量の記載において、特に断りのない限り、%は質量%を意味し、ppmは質量ppmを意味する。また、本発明の球状酸化マグネシウムは、酸化マグネシウム粉末を意図する。 The spherical magnesium oxide of the present invention contains 0.05 to 2.0% titanium and 100 to 1,500 ppm iron, has a volume-based cumulative 50% particle size (D 50 ) in the range of 3 to 200 μm as measured by laser diffraction scattering particle size distribution measurement, and has a sphericity of 1.00 to 1.20 as read from a SEM photograph. In the description of the contents in the specification, % means % by mass, and ppm means ppm by mass, unless otherwise specified. The spherical magnesium oxide of the present invention is intended to be magnesium oxide powder.

 まず、本発明で得られる球状酸化マグネシウムは、レーザー回折散乱式粒度分布測定による体積基準の累積50%粒子径(D50)が3~200μm、好ましくは15~180μm、より好ましくは25μmより大きく150μm以下という放熱性能を高めることができる比較的大きな粒径の範囲であり、かつ真球度が高く充填性に優れる。 First, the spherical magnesium oxide obtained in the present invention has a volume-based cumulative 50% particle size ( D50 ) measured by laser diffraction/scattering particle size distribution measurement of 3 to 200 μm, preferably 15 to 180 μm, and more preferably more than 25 μm and not more than 150 μm, which is a relatively large particle size range capable of improving heat dissipation performance, and also has high sphericity and excellent filling ability.

 本発明において、真球度は、走査型電子顕微鏡(SEM)写真から読み取れる真球度をいい、1.00~1.20、好ましくは1.00~1.15、より好ましくは1.00~1.10とするのがよい。このような真球度であると樹脂への充填性に優れる。なお、本発明においては、SEMを用いて撮影した電子顕微鏡写真の100個の粒子について、粒子の中心を通る長径と短径の長さを計測し、長径/短径の比を求め、その平均値を真球度としている。 In the present invention, sphericity refers to the sphericity that can be read from a scanning electron microscope (SEM) photograph, and should be 1.00 to 1.20, preferably 1.00 to 1.15, and more preferably 1.00 to 1.10. Such sphericity provides excellent filling properties into resin. In the present invention, the lengths of the major and minor axes passing through the center of the particles are measured for 100 particles in an electron microscope photograph taken using an SEM, the ratio of the major axis to the minor axis is calculated, and the average value is taken as the sphericity.

 そして、本発明では、球状酸化マグネシウムのチタン及び鉄の含有量を一定の範囲に調整することで、真球度が高く、樹脂充填時の粘度上昇が小さい球状酸化マグネシウムとすることができる。ここで、チタン含有量は、0.05~2.0%、好ましくは0.08~1.5%、より好ましくは0.1~1.0%とするのがよい。同時に、鉄含有量は、100~1,500ppm、好ましくは150~1,300ppm、より好ましくは200~1,000ppmとするのがよい。チタン及び鉄含有量を適切な量とバランスで配合することによって、真球度が高く、樹脂充填時の粘度上昇が小さい球状酸化マグネシウムとなる。 In the present invention, by adjusting the titanium and iron contents of the spherical magnesium oxide within a certain range, it is possible to obtain spherical magnesium oxide with high sphericity and small viscosity increase when filled with resin. Here, the titanium content is 0.05 to 2.0%, preferably 0.08 to 1.5%, and more preferably 0.1 to 1.0%. At the same time, the iron content is 100 to 1,500 ppm, preferably 150 to 1,300 ppm, and more preferably 200 to 1,000 ppm. By mixing the titanium and iron contents in appropriate amounts and in a balanced manner, spherical magnesium oxide with high sphericity and small viscosity increase when filled with resin can be obtained.

 本発明の球状酸化マグネシウムの製造方法に特に制限はないが、例えば、以下の製造方法により製造することができる:1)塩化マグネシウム水溶液とアルカリ水溶液とを反応させて水酸化マグネシウムスラリーを準備する工程と、2)前記水酸化マグネシウムスラリーを乾燥及び焼成して、酸化マグネシウムを準備する工程と、3)前記酸化マグネシウムを溶媒に分散させ分散液とし、その後湿式粉砕する工程と、4)湿式粉砕後の酸化マグネシウム分散液を噴霧乾燥する工程と、5)噴霧乾燥により造粒した球状酸化マグネシウムを焼成する工程と、を含み、前記1)~5)の少なくとも1つ以上の工程において、焼成後の球状酸化マグネシウムにおけるチタン含有量が0.05~2.0%に、及び鉄含有量が100~1,500ppmになるように、チタン及び/又は鉄の含有量を調整する、球状酸化マグネシウムの製造方法。 The method for producing spherical magnesium oxide of the present invention is not particularly limited, but can be produced, for example, by the following production method: 1) a step of reacting an aqueous magnesium chloride solution with an aqueous alkali solution to prepare magnesium hydroxide slurry, 2) a step of drying and firing the magnesium hydroxide slurry to prepare magnesium oxide, 3) a step of dispersing the magnesium oxide in a solvent to prepare a dispersion liquid, which is then wet-pulverized, 4) a step of spray-drying the magnesium oxide dispersion liquid after wet-pulverization, and 5) a step of firing the spherical magnesium oxide granulated by spray drying, and in at least one or more of the steps 1) to 5), the titanium and/or iron content is adjusted so that the titanium content in the spherical magnesium oxide after firing is 0.05 to 2.0% and the iron content is 100 to 1,500 ppm.

 上記製造方法による場合、より具体的には、以下のようにして製造することができる。
 1)塩化マグネシウム水溶液に、アルカリ水溶液を反応させて水酸化マグネシウムスラリーを得、次いで、
 2)スラリーを濾過、水洗、乾燥させた後焼成し、酸化マグネシウムを得、
 3)前記酸化マグネシウムを溶媒、好ましくは有機溶媒に分散させ分散液とし、湿式粉砕を行った後、
 4)噴霧乾燥を行い、
 5)得られた球状酸化マグネシウムを焼成することで、目的の球状酸化マグネシウムを得る。このとき、最終焼成までに、最終焼成後の球状酸化マグネシウムのチタン含有量が0.05~2.0%及び鉄含有量が100~1,500ppmになるようチタン源及び/又は鉄源を混合及び/又は添加等で調整する。チタン含有量及び/又は鉄源の調整は、具体的には、例えば、a)塩化マグネシウム水溶液及び/又はアルカリ水溶液中にホウ素源及び/又は鉄源を添加する、b)生成した水酸化マグネシウムスラリーにチタン源及び/又は鉄源を添加する、c)水酸化マグネシウムを焼成することで得た酸化マグネシウムにチタン源及び/又は鉄源を混合する、d)酸化マグネシウムの湿式粉砕中にチタン源及び/又は鉄源を添加する、e)噴霧乾燥により造粒した球状酸化マグネシウムにチタン源及び/又は鉄源を混合する、等の方法で最終的に得られる球状酸化マグネシウム中のチタン含有量及び鉄含有量を調整する。なお、チタン含有量及び鉄含有量は、同一の工程において調整してもよいし、異なる工程において調整してもよい。
More specifically, the above-mentioned production method can be carried out as follows.
1) A magnesium chloride aqueous solution is reacted with an alkaline aqueous solution to obtain a magnesium hydroxide slurry, and then
2) The slurry is filtered, washed with water, dried, and then calcined to obtain magnesium oxide.
3) The magnesium oxide is dispersed in a solvent, preferably an organic solvent, to obtain a dispersion liquid, which is then wet-pulverized.
4) Spray drying is carried out;
5) The obtained spherical magnesium oxide is fired to obtain the desired spherical magnesium oxide. At this time, a titanium source and/or an iron source are mixed and/or added before the final firing so that the titanium content of the spherical magnesium oxide after the final firing is 0.05 to 2.0% and the iron content is 100 to 1,500 ppm. Specifically, the titanium content and/or the iron source are adjusted by, for example, a) adding a boron source and/or an iron source to an aqueous magnesium chloride solution and/or an alkaline aqueous solution, b) adding a titanium source and/or an iron source to the generated magnesium hydroxide slurry, c) mixing a titanium source and/or an iron source with magnesium oxide obtained by firing magnesium hydroxide, d) adding a titanium source and/or an iron source during wet grinding of magnesium oxide, e) mixing a titanium source and/or an iron source with spherical magnesium oxide granulated by spray drying, or the like, to adjust the titanium content and iron content in the spherical magnesium oxide finally obtained. The titanium content and the iron content may be adjusted in the same process or in different processes.

 チタン源としてはチタンを含む化合物であれば特に限定されないが、例えば、酸化チタン(アナターゼ型、ルチル型)、塩化チタン、水酸化チタン、臭化チタン、フッ化チタン、チタン酸マグネシウム等が挙げられる。 The titanium source is not particularly limited as long as it is a compound containing titanium, but examples include titanium oxide (anatase type, rutile type), titanium chloride, titanium hydroxide, titanium bromide, titanium fluoride, magnesium titanate, etc.

 鉄源としては鉄を含む化合物であれば特に限定されないが、例えば、酸化鉄(II)、酸化鉄(III)、四三酸化鉄、水酸化鉄、塩化鉄、窒化鉄、臭化鉄、フッ化鉄等が挙げられる。 The iron source is not particularly limited as long as it is a compound containing iron, but examples include iron oxide (II), iron oxide (III), iron tetroxide, iron hydroxide, iron chloride, iron nitride, iron bromide, and iron fluoride.

 最終焼成後の球状酸化マグネシウムのチタン含有量が0.05~2.0%になるようチタン源を調整する。チタン含有量が0.05%未満の場合は、粘度の低下の効果が十分に得られない。また、チタン含有量が2.0%を超える場合は、粒子の過剰な成長や粒子同士の固着がおきやすくなるため、真球度が高い球状酸化マグネシウムを得ることができない。そして、最終焼成後の球状酸化マグネシウムの鉄含有量が100~1,500ppmになるよう鉄源を調整する。上記チタン含有量に加え、鉄含有量が100~1,500ppmの範囲にあると、真球度が高い球状酸化マグネシウムとなる傾向にある。 The titanium source is adjusted so that the titanium content of the spherical magnesium oxide after final firing is 0.05-2.0%. If the titanium content is less than 0.05%, the effect of reducing viscosity is not sufficient. Furthermore, if the titanium content exceeds 2.0%, excessive particle growth and adhesion between particles are likely to occur, making it impossible to obtain spherical magnesium oxide with high sphericity. Then, the iron source is adjusted so that the iron content of the spherical magnesium oxide after final firing is 100-1,500 ppm. In addition to the above titanium content, if the iron content is in the range of 100-1,500 ppm, spherical magnesium oxide with high sphericity tends to be obtained.

 上記塩化マグネシウム水溶液は、例えば、塩化マグネシウム六水和物、塩化マグネシウム二水和物、塩化マグネシウム無水和物、苦汁(にがり)、海水等、及びこれらの組合せから選択して用いることができる。 The magnesium chloride aqueous solution can be selected from, for example, magnesium chloride hexahydrate, magnesium chloride dihydrate, anhydrous magnesium chloride, bittern, seawater, and combinations thereof.

 上記アルカリ水溶液としては、例えば、水酸化ナトリウム水溶液、水酸化カルシウム水溶液、アンモニア水等、及びこれらの組合せから選択して用いることができる。 The alkaline aqueous solution can be selected from, for example, an aqueous sodium hydroxide solution, an aqueous calcium hydroxide solution, ammonia water, and combinations thereof.

 塩化マグネシウム水溶液とアルカリ水溶液とを反応させて得た水酸化マグネシウムスラリーは、例えば当該技術分野における一般的な方法によって、濾過、水洗、乾燥させた後焼成し、酸化マグネシウムとする。そして、得られる酸化マグネシウムは、溶媒に分散させて分散液(例えばスラリー)とし、これを湿式粉砕し、噴霧乾燥することで、造粒する。このときの溶媒は特に限定されないが、例えば、水系、水-有機溶媒混合系、メタノール、エタノール等のアルコール類、アセトン等のケトン類、酢酸エチル等のエステル類、ジエチルエーテル等のエーテル類、テトラヒドロフラン、トルエンなどの芳香族化合物溶媒など、公知に用いられている溶媒を使用できる。 The magnesium hydroxide slurry obtained by reacting an aqueous magnesium chloride solution with an aqueous alkali solution is filtered, washed with water, dried, and then calcined to form magnesium oxide, for example, by a method common in the technical field. The obtained magnesium oxide is then dispersed in a solvent to form a dispersion (for example, a slurry), which is wet-pulverized and spray-dried to form granules. The solvent used here is not particularly limited, but any known solvent can be used, such as water-based systems, water-organic solvent mixtures, alcohols such as methanol and ethanol, ketones such as acetone, esters such as ethyl acetate, ethers such as diethyl ether, and aromatic compound solvents such as tetrahydrofuran and toluene.

 噴霧乾燥の方法は特に限定されないが、例えば、湿式粉砕後の酸化マグネシウム分散液(例えばスラリー)を回転ディスクやノズルから噴霧し、酸化マグネシウム粒子を得るスプレードライ法等を用いることが好ましい。操作条件は、スラリー粘度やスラリー中の粉体の粒度、目的とする粒子径等に応じて適宜調整する。また、スラリーには分散剤を適宜加えても良い。その操作条件は特に限定するものではないが、スプレードライ法の場合、例えば、回転ディスクやノズルより、粘度を10~3000cpsに調整したスラリーを、流量を適宜調節して80℃~250℃の気流中に噴霧し、1~200μm程度の粒子を製造することができる。また、湿式粉砕及び噴霧時の分散液の濃度は、例えば、酸化マグネシウムが50~70wt%になるように調整するのが好ましい。ここで、噴霧条件を適切に設定することで、得られる球状酸化マグネシウムの真球度を調整することができる。また、噴霧条件を適切に設定することで、得られる球状酸化マグネシウムの累積50%粒子径(D50)を調整することができる。スプレードライ法は、粒径の大きい粒子を安定的に得られることから好ましい。 The method of spray drying is not particularly limited, but it is preferable to use a spray drying method in which a magnesium oxide dispersion (e.g., a slurry) after wet grinding is sprayed from a rotating disk or nozzle to obtain magnesium oxide particles. The operating conditions are appropriately adjusted according to the slurry viscosity, the particle size of the powder in the slurry, the target particle size, and the like. In addition, a dispersant may be appropriately added to the slurry. The operating conditions are not particularly limited, but in the case of the spray drying method, for example, a slurry with a viscosity adjusted to 10 to 3000 cps is sprayed from a rotating disk or nozzle into an air flow at 80°C to 250°C by appropriately adjusting the flow rate, and particles of about 1 to 200 μm can be produced. In addition, it is preferable to adjust the concentration of the dispersion during wet grinding and spraying so that, for example, magnesium oxide is 50 to 70 wt %. Here, by appropriately setting the spray conditions, the sphericity of the obtained spherical magnesium oxide can be adjusted. In addition, by appropriately setting the spray conditions, the cumulative 50% particle size (D 50 ) of the obtained spherical magnesium oxide can be adjusted. The spray drying method is preferred since it can stably obtain particles having a large particle size.

 造粒した酸化マグネシウムの焼成条件は酸化マグネシウム粒子が焼結する範囲であれば特に限定されないが、温度を1000℃~1800℃とするのが好ましく、1100℃~1700℃とするのがより好ましく、1200℃~1600℃とするのが特に好ましい。焼成時間は焼成温度によるが、0.5~10時間であることが好ましい。焼成温度は1000℃に満たないと、十分に焼結せず、1800℃を超えると、粒子同士が焼結し粗大な凝集体を形成するから上記の範囲に調整する。 The conditions for sintering the granulated magnesium oxide are not particularly limited as long as they are within the range in which the magnesium oxide particles are sintered, but a temperature of 1000°C to 1800°C is preferable, 1100°C to 1700°C is more preferable, and 1200°C to 1600°C is particularly preferable. The sintering time depends on the sintering temperature, but is preferably 0.5 to 10 hours. If the sintering temperature is less than 1000°C, sufficient sintering will not occur, and if it exceeds 1800°C, the particles will sinter together and form coarse agglomerates, so it is adjusted to the above range.

 本発明の球状酸化マグネシウムは、耐湿性を改善する目的で公知の方法を用いて表面処理を施すこともできる。本発明の球状酸化マグネシウムに表面処理を施すにあたり、使用する表面処理剤は特に限定されないが、例えば、コロイダルシリカ、シラン系カップリング剤、チタニアゾル、チタネート系カップリング剤、リン化合物、アルミナゾル、アルミネート系カップリング剤、ジルコニウム系カップリング剤等を用いることができる。これらは単独で使用してもよいし、2種以上を併用してもよい。 The spherical magnesium oxide of the present invention can also be surface-treated using a known method for the purpose of improving moisture resistance. When surface-treating the spherical magnesium oxide of the present invention, there are no particular limitations on the surface treatment agent used, but examples that can be used include colloidal silica, silane-based coupling agents, titania sol, titanate-based coupling agents, phosphorus compounds, alumina sol, aluminate-based coupling agents, zirconium-based coupling agents, etc. These may be used alone or in combination of two or more types.

 シラン系カップリング剤としては、例えば、ビニルトリクロルシラン、ビニルトリアルコキシシラン、グリシドキシプロピルトリアルコキシシラン、メタクロキシプロピルメチルジアルコキシシラン等があげられる。 Examples of silane coupling agents include vinyltrichlorosilane, vinyltrialkoxysilane, glycidoxypropyltrialkoxysilane, and methacryloxypropylmethyldialkoxysilane.

 チタネート系カップリング剤としては、例えば、テトライソプロピルチタネート、テトラノルマルブチルチタネート、テトラオクチルチタネート、テトラステアリルチタネート、イソプロピルトリイソステアロイルチタネート、テトラオクチルビス(ジトリデシルホスファイト)チタネート、ビス(ジオクチルパイロホスフェート)オキシアセテートチタネート等があげられる。 Titanate coupling agents include, for example, tetraisopropyl titanate, tetranormalbutyl titanate, tetraoctyl titanate, tetrastearyl titanate, isopropyltriisostearoyl titanate, tetraoctylbis(ditridecylphosphite)titanate, bis(dioctylpyrophosphate)oxyacetate titanate, etc.

 リン化合物としては、酸化マグネシウムと反応してリン酸マグネシウム系化合物を形成し得る化合物であれば特に限定されないが、例えば、リン酸、リン酸塩、酸性リン酸エステルが挙げられる。酸性リン酸エステルとしては、例えば、イソプロピルアシッドホスフェート、2-エチルヘキシルアシッドホスフェート、オレイルアシッドホスフェート、メチルアシッドホスフェート、エチルアシッドホスフェート、プロピルアシッドホスフェート、ブチルアシッドホスフェート、ラウリルアシッドホスフェート、ステアリルアシッドホスフェートが挙げられる。 The phosphorus compound is not particularly limited as long as it is a compound that can react with magnesium oxide to form a magnesium phosphate compound, but examples include phosphoric acid, phosphates, and acidic phosphate esters. Examples of acidic phosphate esters include isopropyl acid phosphate, 2-ethylhexyl acid phosphate, oleyl acid phosphate, methyl acid phosphate, ethyl acid phosphate, propyl acid phosphate, butyl acid phosphate, lauryl acid phosphate, and stearyl acid phosphate.

 アルミネート系カップリング剤としては、例えば、アルミニウムイソプロピレート、モノsec-ブトキシアルミニウムジイソプロピレート、アルミニウムsec-ブチレート、アルミニウムエチルアセトアセテートジイソプロピレート、アルミニウムトリス(エチルアセトアセテート)、アルミニウムアルキルアセトアセテートジイソプロピレートがあげられる。 Examples of aluminate coupling agents include aluminum isopropylate, monosec-butoxyaluminum diisopropylate, aluminum sec-butylate, aluminum ethyl acetoacetate diisopropylate, aluminum tris(ethyl acetoacetate), and aluminum alkyl acetoacetate diisopropylate.

 ジルコニウム系カップリング剤としては、例えば、ノルマルプロピルジルコネート、ノルマルブチルジルコネート等があげられる。 Examples of zirconium-based coupling agents include normal propyl zirconate and normal butyl zirconate.

 本発明の球状酸化マグネシウムは、真球度が高く充填性に優れ、かつ樹脂充填時の粘度上昇が小さいという利点があるため、好適に充填材として樹脂に配合することができ、熱伝導性フィラーとして有用である。本発明の熱伝導性フィラーは、本発明の球状酸化マグネシウムを単独で含有するものであってもよいし、本発明の球状酸化マグネシウムと共にそれ以外の熱伝導性フィラー材料を含有するものであってもよい。本発明の樹脂組成物には、本発明の熱伝導性フィラーが配合され、本発明で使用可能な樹脂としては、例えば、熱硬化性樹脂、又は熱可塑性樹脂が挙げられる。熱硬化性樹脂としては特に限定されないが、例えば、フェノール樹脂、尿素樹脂、メラミン樹脂、アルキド樹脂、ポリエステル樹脂、エポキシ樹脂、ジアリルフタレート樹脂、ポリウレタン樹脂、シリコーン樹脂等が挙げられる。熱可塑性樹脂としては特に限定されないが、例えば、ポリアミド樹脂、ポリアセタール樹脂、ポリカーボネート樹脂、ポリブチレンテレフタレート樹脂、ポリオレフィン樹脂、ポリスルフォン樹脂、ポリアミドイミド樹脂、ポリエーテルイミド樹脂、ポリアリレート樹脂、ポリフェニレンスルフィド樹脂、ポリエーテルエーテルケトン樹脂、フッ素樹脂、液晶ポリマー等が挙げられる。 The spherical magnesium oxide of the present invention has the advantages of high sphericity, excellent filling properties, and small increase in viscosity when filled into resin, and can therefore be suitably blended into resin as a filler, making it useful as a thermally conductive filler. The thermally conductive filler of the present invention may contain the spherical magnesium oxide of the present invention alone, or may contain the spherical magnesium oxide of the present invention together with other thermally conductive filler materials. The resin composition of the present invention contains the thermally conductive filler of the present invention, and examples of resins that can be used in the present invention include thermosetting resins and thermoplastic resins. Thermosetting resins are not particularly limited, but examples include phenolic resins, urea resins, melamine resins, alkyd resins, polyester resins, epoxy resins, diallyl phthalate resins, polyurethane resins, and silicone resins. Thermoplastic resins are not particularly limited, but examples include polyamide resins, polyacetal resins, polycarbonate resins, polybutylene terephthalate resins, polyolefin resins, polysulfone resins, polyamideimide resins, polyetherimide resins, polyarylate resins, polyphenylene sulfide resins, polyether ether ketone resins, fluororesins, and liquid crystal polymers.

 本発明の樹脂組成物における球状酸化マグネシウムの配合量は、樹脂組成物に求められる特性に応じて適宜決定すればよく、特に限定されない。しかし、一例として樹脂100質量部に対し、球状酸化マグネシウム0.1~100質量部の範囲で使用すればよい。 The amount of spherical magnesium oxide in the resin composition of the present invention may be appropriately determined depending on the properties required of the resin composition, and is not particularly limited. However, as an example, spherical magnesium oxide may be used in the range of 0.1 to 100 parts by mass per 100 parts by mass of resin.

 本発明の球状酸化マグネシウムを含む樹脂組成物は、その樹脂の特性に応じて種々の分野で利用することができる。しかし、本発明の球状酸化マグネシウムは熱伝導性に優れていることから、特に放熱性が要求される用途で好適に使用することができる。例えば、本発明の樹脂組成物は、熱伝導性に優れた半導体封止材料として利用することができる。 The resin composition containing the spherical magnesium oxide of the present invention can be used in various fields depending on the characteristics of the resin. However, since the spherical magnesium oxide of the present invention has excellent thermal conductivity, it can be used particularly preferably in applications where heat dissipation is required. For example, the resin composition of the present invention can be used as a semiconductor encapsulation material with excellent thermal conductivity.

 下記の実施例により本発明を詳細に説明するが、これらの実施例は本発明をいかなる意味においても制限するものではない。 The present invention will be described in detail with reference to the following examples, but these examples are not intended to limit the present invention in any way.

[測定方法・評価方法]
(1)鉄含有量の測定方法
 鉄含有量の測定は、ICP発光分光分析により行った。測定試料を、12Nの塩酸(試薬特級)に加え加熱して完全に溶解させた後、ICP測定装置(PS3520 VDD、株式会社日立ハイテクサイエンス製)を用いて含有量を測定した。
[Measurement and evaluation methods]
(1) Measurement method of iron content The iron content was measured by ICP emission spectrometry. The measurement sample was added to 12N hydrochloric acid (special grade reagent) and heated to completely dissolve, and the iron content was measured using an ICP measurement device (PS3520 VDD, manufactured by Hitachi High-Tech Science Corporation).

(2)チタン含有量の測定方法
 チタン含有量の測定は、蛍光X線分析装置(装置名:ZSX Primus4、株式会社リガク製)により行った。まず、測定対象の酸化マグネシウムを、アルミリング(φ35mm)に入れ、ダイスで挟み、プレス機(面圧250MPa)にかけてペレット化することにより測定用試料を得た。この試料を、SQX分析(EZスキャン)(管球:Rh(4kW)、雰囲気:真空、分析窓:Be(30μm)、測定径:30mmφ、測定範囲F~U)モードで測定し、酸化マグネシウム中のチタン含有量を求めた。
(2) Measurement method of titanium content The titanium content was measured using an X-ray fluorescence analyzer (device name: ZSX Primus4, manufactured by Rigaku Corporation). First, the magnesium oxide to be measured was placed in an aluminum ring (φ35 mm), sandwiched between dies, and pelletized using a press (surface pressure 250 MPa) to obtain a measurement sample. This sample was measured in SQX analysis (EZ scan) mode (bulb: Rh (4 kW), atmosphere: vacuum, analysis window: Be (30 μm), measurement diameter: 30 mmφ, measurement range F to U) to determine the titanium content in the magnesium oxide.

(3)体積基準の累積50%粒子径(D50
 測定試料0.1×10-3kgを精密に秤量し、40mLのメタノールで分散し、レーザー回折散乱式粒度分布測定装置(MT3300 日機装株式会社製)を用いて測定した。
(3) Volume-based cumulative 50% particle size ( D50 )
0.1×10 −3 kg of the measurement sample was precisely weighed, dispersed in 40 mL of methanol, and measured using a laser diffraction scattering type particle size distribution measuring device (MT3300, manufactured by Nikkiso Co., Ltd.).

(4)SEM写真から読み取れる真球度
 走査型電子顕微鏡(SEM)(JSM6510LA 日本電子株式会社製)を用いて評価対象の酸化マグネシウムを撮影した。無作為に選択した電子顕微鏡写真の100個の粒子について、粒子の中心を通る長径と短径の長さを計測し、長径/短径の比を求め、その平均値を真球度とした。
(4) Sphericity as seen from SEM photographs Magnesium oxide samples were photographed using a scanning electron microscope (SEM) (JSM6510LA, manufactured by JEOL Ltd.) The major and minor axes passing through the center of the particles were measured for 100 randomly selected particles in the electron microscope photographs, and the ratio of the major axis to the minor axis was calculated, and the average value was taken as the sphericity.

(5)樹脂充填時の粘度評価
 評価対象の球状酸化マグネシウムと、アルミナ粒子(デンカ社製「DAW-05」(平均粒子径:5μm))を50体積%ずつ混合し、これをシリコーンオイル(信越化学工業社製「KF96-100cs」)に、球状酸化マグネシウムとアルミナ粒子との合計の充填率が75体積%となるように投入した。これを自転・公転ミキサーを用いて回転数2,200rpmで30秒間混合後、真空脱泡して樹脂組成物を得た。得られた樹脂組成物について、粘度をB型粘度計(TOKIMEC社製BL型、測定条件:試料温度25℃、6rpm、ローターNo.4、容器寸法φ26mm×h46mm、試料量20mL)を用いて測定した。
(5) Viscosity evaluation during resin filling Spherical magnesium oxide to be evaluated and alumina particles (Denka's "DAW-05" (average particle size: 5 μm)) were mixed at 50% by volume, and this was added to silicone oil (Shin-Etsu Chemical's "KF96-100cs") so that the total filling rate of the spherical magnesium oxide and alumina particles was 75% by volume. This was mixed for 30 seconds at a rotation speed of 2,200 rpm using a rotation/revolution mixer, and then vacuum degassed to obtain a resin composition. The viscosity of the obtained resin composition was measured using a B-type viscometer (TOKIMEC's BL type, measurement conditions: sample temperature 25°C, 6 rpm, rotor No. 4, container dimensions φ26 mm × h46 mm, sample amount 20 mL).

[実施例および比較例]
(実施例1)
 無水塩化マグネシウム(MgCl)をイオン交換水に溶解して、約3.5mol/lの塩化マグネシウム水溶液を調製した。MgClの反応率が90モル%になるよう、MgCl溶液と25%NaOH溶液をそれぞれ定量ポンプでリアクターに送液して、連続反応を実施し、水酸化マグネシウムスラリーを得た。その後、水酸化マグネシウムスラリーに最終的に得られる球状酸化マグネシウム中のチタン含有量が0.7%となるよう酸化チタン/アナタ―ゼ型(テイカ株式会社製、JA-20)を、鉄含有量が250ppmとなるよう酸化鉄(II)(林純薬工業株式会社製)を添加した。その後濾過、水洗、乾燥し、水酸化マグネシウムを得た。得られた水酸化マグネシウムを900℃で1時間焼成し、酸化マグネシウムを得た。得られた酸化マグネシウムを、有機溶媒に分散させ、酸化マグネシウム濃度が65wt%のスラリーを得た。その後ボールミルを用いて4時間、湿式粉砕を行った後、スプレードライ法による噴霧乾燥を行った。得られた噴霧乾燥後の球状酸化マグネシウムを、電気炉を用いて1400℃、1時間最終焼成し、目的の球状酸化マグネシウムを得た。
[Examples and Comparative Examples]
Example 1
Anhydrous magnesium chloride (MgCl 2 ) was dissolved in ion-exchanged water to prepare an aqueous magnesium chloride solution of about 3.5 mol/l. The MgCl 2 solution and 25% NaOH solution were each pumped into a reactor with a metering pump so that the reaction rate of MgCl 2 was 90 mol%, and a continuous reaction was carried out to obtain a magnesium hydroxide slurry. Then, titanium oxide/anatase type (manufactured by Teika Co., Ltd., JA-20) was added to the magnesium hydroxide slurry so that the titanium content in the spherical magnesium oxide finally obtained was 0.7%, and iron oxide (II) (manufactured by Hayashi Pure Chemical Industries Co., Ltd.) was added so that the iron content was 250 ppm. Then, the mixture was filtered, washed with water, and dried to obtain magnesium hydroxide. The obtained magnesium hydroxide was fired at 900°C for 1 hour to obtain magnesium oxide. The obtained magnesium oxide was dispersed in an organic solvent to obtain a slurry with a magnesium oxide concentration of 65 wt%. Then, wet grinding was performed using a ball mill for 4 hours, and spray drying was performed by a spray drying method. The resulting spray-dried spherical magnesium oxide was finally fired in an electric furnace at 1400° C. for 1 hour to obtain the desired spherical magnesium oxide.

(実施例2)
 反応液に、球状酸化マグネシウム中のチタン量が0.39%となるよう酸化チタンを、鉄含有量が330ppmとなるよう酸化鉄(II)を添加した以外は、実施例1と同様の製法を用いて、球状酸化マグネシウムを得た。
Example 2
Spherical magnesium oxide was obtained using the same production method as in Example 1, except that titanium oxide was added to the reaction liquid so that the titanium content in the spherical magnesium oxide was 0.39% and iron (II) oxide was added to the reaction liquid so that the iron content was 330 ppm.

(実施例3)
 反応液に、球状酸化マグネシウム中のチタン量が0.11%となるよう酸化チタンを、鉄含有量が330ppmとなるよう酸化鉄(II)を添加した以外は、実施例1と同様の製法を用いて、球状酸化マグネシウムを得た。
Example 3
Spherical magnesium oxide was obtained using the same production method as in Example 1, except that titanium oxide was added to the reaction liquid so that the titanium content in the spherical magnesium oxide was 0.11% and iron (II) oxide was added to the reaction liquid so that the iron content was 330 ppm.

(実施例4)
 反応液に、球状酸化マグネシウム中のチタン量が0.75%となるよう酸化チタンを、鉄含有量が240ppmとなるよう酸化鉄(II)を添加し、最終焼成時の焼成温度を1300℃とした以外は、実施例1と同様の製法を用いて、球状酸化マグネシウムを得た。
Example 4
Spherical magnesium oxide was obtained using the same manufacturing method as in Example 1, except that titanium oxide was added to the reaction solution so that the titanium content in the spherical magnesium oxide was 0.75% and iron (II) oxide was added so that the iron content was 240 ppm, and the firing temperature in the final firing was 1300°C.

(比較例1)
 反応液に、チタン源は添加せず、鉄含有量が240ppmとなるよう酸化鉄(II)を添加した以外は、実施例1と同様の製法を用いて、球状酸化マグネシウムを得た。
(Comparative Example 1)
Spherical magnesium oxide was obtained in the same manner as in Example 1, except that no titanium source was added to the reaction solution, and iron (II) oxide was added so that the iron content was 240 ppm.

 実施例1~4及び比較例1について、上記の測定及び評価を行った。結果を表1に示す。 The above measurements and evaluations were carried out for Examples 1 to 4 and Comparative Example 1. The results are shown in Table 1.

Figure JPOXMLDOC01-appb-T000001
Figure JPOXMLDOC01-appb-T000001

 表1から明らかなように、実施例1~4の球状酸化マグネシウムは、真球度が高く、また樹脂充填時の粘度上昇が低く抑えられていた。一方、比較例1の球状酸化マグネシウムは、真球度は高いものの、樹脂充填時の粘度上昇が大きく、フィラーとしての性能が劣っていた。 As is clear from Table 1, the spherical magnesium oxide of Examples 1 to 4 had high sphericity and the increase in viscosity when filled with resin was kept low. On the other hand, the spherical magnesium oxide of Comparative Example 1 had high sphericity, but the increase in viscosity when filled with resin was large, and its performance as a filler was poor.

 これより、本発明の球状酸化マグネシウムは、樹脂充填時の粘度上昇が小さく、かつ真球度が高く樹脂への充填性に優れることがわかった。よって、本発明の球状酸化マグネシウムは、優れた樹脂フィラーとして有用であることがわかった。 From this, it was found that the spherical magnesium oxide of the present invention has a small increase in viscosity when filled into resin, has high sphericity, and is excellent in fillability into resin. Therefore, it was found that the spherical magnesium oxide of the present invention is useful as an excellent resin filler.

 本発明によれば、樹脂充填時の粘度上昇が小さく、かつ真球度が高く樹脂への充填性に優れる球状酸化マグネシウム及びその製造方法を提供することができる。 The present invention provides spherical magnesium oxide that exhibits a small increase in viscosity when filled into resin, has high sphericity, and is excellent in fillability into resin, as well as a method for producing the same.

Claims (5)

 チタン0.05~2.0%及び鉄100~1,500ppmを含有し、レーザー回折散乱式粒度分布測定による体積基準の累積50%粒子径(D50)が3~200μmの範囲であり、SEM写真から読み取れる真球度が1.00~1.20である、球状酸化マグネシウム。 The present invention relates to a spherical magnesium oxide having a volume-based cumulative 50% particle size (D 50 ) in the range of 3 to 200 μm as measured by a laser diffraction/scattering particle size distribution measurement, and a sphericity of 1.00 to 1.20 as measured by a SEM photograph.  累積50%粒子径(D50)が、25μmより大きく150μm以下である、請求項1記載の球状酸化マグネシウム。 The spherical magnesium oxide according to claim 1, having a cumulative 50% particle size (D 50 ) of more than 25 μm and not more than 150 μm.  請求項1又は2記載の球状酸化マグネシウムを含有する熱伝導性フィラー。 A thermally conductive filler containing the spherical magnesium oxide according to claim 1 or 2.  請求項3記載の熱伝導性フィラーを含有する樹脂組成物。 A resin composition containing the thermally conductive filler according to claim 3.  1)塩化マグネシウム水溶液とアルカリ水溶液とを反応させて水酸化マグネシウムスラリーを準備する工程と、
2)前記水酸化マグネシウムスラリーを乾燥及び焼成して、酸化マグネシウムを準備する工程と、
3)前記酸化マグネシウムを溶媒に分散させ分散液とし、その後湿式粉砕する工程と、
4)湿式粉砕後の酸化マグネシウム分散液を噴霧乾燥する工程と、
5)噴霧乾燥により造粒した球状酸化マグネシウムを焼成する工程と、
を含み、
前記1)~5)の少なくとも1つ以上の工程において、焼成後の球状酸化マグネシウムにおけるチタン含有量が0.05~2.0%に、及び鉄含有量が100~1,500ppmになるように、チタン及び/又は鉄の含有量を調整する、
球状酸化マグネシウムの製造方法。
1) reacting an aqueous magnesium chloride solution with an aqueous alkali solution to prepare a magnesium hydroxide slurry;
2) drying and calcining the magnesium hydroxide slurry to prepare magnesium oxide;
3) dispersing the magnesium oxide in a solvent to obtain a dispersion liquid, and then wet-grinding the dispersion liquid;
4) spray-drying the magnesium oxide dispersion after wet grinding;
5) Calcining the spherical magnesium oxide granulated by spray drying;
Including,
In at least one of the steps 1) to 5), the titanium and/or iron content is adjusted so that the titanium content in the spherical magnesium oxide after firing is 0.05 to 2.0% and the iron content is 100 to 1,500 ppm.
A method for producing spherical magnesium oxide.
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Citations (6)

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JP2017122029A (en) * 2016-01-07 2017-07-13 協和化学工業株式会社 Magnesium hydroxide particles having a slow growth rate and a low aspect ratio and method for producing the same
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JP2022048574A (en) * 2020-09-15 2022-03-28 デンカ株式会社 Magnesium oxide powder, filler composition, resin composition, and heat dissipating component
JP2022048542A (en) * 2020-09-15 2022-03-28 デンカ株式会社 Magnesium oxide powder, filler composition, resin composition, and heat dissipating component
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JP2012201511A (en) * 2011-03-23 2012-10-22 Tateho Chemical Industries Co Ltd Spherical magnesium hydroxide particle, spherical magnesium oxide particle, and method for producing them
JP2017122029A (en) * 2016-01-07 2017-07-13 協和化学工業株式会社 Magnesium hydroxide particles having a slow growth rate and a low aspect ratio and method for producing the same
JP2022502340A (en) * 2018-08-09 2022-01-11 ジョイント ストック カンパニー コースティック Active high-purity magnesium oxide and its manufacturing method
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