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JP7717680B2 - Method for producing silicon nitride powder and silicon nitride sintered body - Google Patents
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JP7717680B2 - Method for producing silicon nitride powder and silicon nitride sintered body - Google Patents

Method for producing silicon nitride powder and silicon nitride sintered body

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JP7717680B2
JP7717680B2 JP2022512238A JP2022512238A JP7717680B2 JP 7717680 B2 JP7717680 B2 JP 7717680B2 JP 2022512238 A JP2022512238 A JP 2022512238A JP 2022512238 A JP2022512238 A JP 2022512238A JP 7717680 B2 JP7717680 B2 JP 7717680B2
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silicon nitride
nitride powder
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敏行 宮下
祐三 中村
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Denka Co Ltd
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Denki Kagaku Kogyo KK
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    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B21/00Nitrogen; Compounds thereof
    • C01B21/06Binary compounds of nitrogen with metals, with silicon, or with boron, or with carbon, i.e. nitrides; Compounds of nitrogen with more than one metal, silicon or boron
    • C01B21/068Binary compounds of nitrogen with metals, with silicon, or with boron, or with carbon, i.e. nitrides; Compounds of nitrogen with more than one metal, silicon or boron with silicon
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    • C04B35/00Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/515Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on non-oxide ceramics
    • C04B35/58Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on non-oxide ceramics based on borides, nitrides, i.e. nitrides, oxynitrides, carbonitrides or oxycarbonitrides or silicides
    • C04B35/584Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on non-oxide ceramics based on borides, nitrides, i.e. nitrides, oxynitrides, carbonitrides or oxycarbonitrides or silicides based on silicon nitride

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Description

本開示は、窒化ケイ素粉末、及び窒化ケイ素焼結体の製造方法に関する。 The present disclosure relates to a silicon nitride powder and a method for producing a silicon nitride sintered body.

窒化ケイ素は、強度、硬度、靭性、耐熱性、耐食性、耐熱衝撃性等に優れた材料であることから、ダイカストマシン及び溶解炉等の各種産業用の部品、及び自動車部品等に利用されている。また、窒化ケイ素は、高温における機械的特性にも優れることから、高温強度、高温クリープ特性が求められるガスタービン部品に適用することが検討されている。例えば、特許文献1では、窒化ケイ素焼結体の高温特性を向上させる方法として、窒化ケイ素粉末の全酸素量を1.5質量%以下にして、焼結時に精製する粒界相を低減し、融点を高く維持して高温特性を向上することが検討されている。 Silicon nitride is a material with excellent strength, hardness, toughness, heat resistance, corrosion resistance, and thermal shock resistance, and is therefore used in various industrial parts such as die-casting machines and melting furnaces, as well as automotive parts. Furthermore, because silicon nitride also has excellent mechanical properties at high temperatures, its application to gas turbine parts, which require high-temperature strength and high-temperature creep properties, is being considered. For example, Patent Document 1 considers a method for improving the high-temperature properties of silicon nitride sintered bodies by reducing the total oxygen content of the silicon nitride powder to 1.5 mass% or less, thereby reducing the grain boundary phase refined during sintering and maintaining a high melting point, thereby improving high-temperature properties.

窒化ケイ素焼結体には、熱伝導率及び機械的特性の更なる向上が求められている。例えば、特許文献2では、常温における熱伝導率が100~300W/(m・K)であり、常温における3点曲げ強度が600~1500MPaであることを特徴とする窒化珪素質焼結体が記載されている。 Further improvements in thermal conductivity and mechanical properties are required for silicon nitride sintered bodies. For example, Patent Document 2 describes a silicon nitride sintered body characterized by a thermal conductivity of 100 to 300 W/(m·K) at room temperature and a three-point bending strength of 600 to 1500 MPa at room temperature.

また特許文献3には、比表面積が4.0~9.0m/gであり、β相の割合が40質量%より小さく、酸素含有量が0.20~0.95質量%であり、レーザー回折散乱法による体積基準の粒度分布測定により得られる頻度分布曲線が、二つのピークを有し、該ピークのピークトップが、0.4~0.7μmの範囲と、1.5~3.0μmの範囲にあり、前記ピークトップの頻度の比(粒子径0.4~0.7μmの範囲のピークトップの頻度/粒子径1.5~3.0μmの範囲のピークトップの頻度)が0.5~1.5であり、前記粒度分布測定により得られるメディアン径D50(μm)と上記比表面積より算出される比表面積相当径DBET(μm)との比D50/DBET(μm/μm)が3.5以上であることを特徴とする窒化ケイ素粉末が記載されている。 Patent Document 3 describes a silicon nitride powder characterized by having a specific surface area of 4.0 to 9.0 m2 /g, a β-phase ratio of less than 40 mass%, an oxygen content of 0.20 to 0.95 mass%, a frequency distribution curve obtained by volumetric particle size distribution measurement using a laser diffraction scattering method having two peaks with peak tops in the ranges of 0.4 to 0.7 μm and 1.5 to 3.0 μm, a frequency ratio of the peak tops (frequency of peak tops in the particle size range of 0.4 to 0.7 μm/frequency of peak tops in the particle size range of 1.5 to 3.0 μm) of 0.5 to 1.5, and a ratio D50/DBET (μm/μm) of the median diameter D50 (μm) obtained by the particle size distribution measurement to the specific surface area equivalent diameter DBET (μm) calculated from the specific surface area, of 3.5 or more.

特開平7-206409号公報Japanese Patent Application Publication No. 7-206409 特開2004-262756号公報Japanese Patent Application Laid-Open No. 2004-262756 国際公開第2015/194552号International Publication No. 2015/194552

本開示は、熱伝導率及び曲げ強度に優れる焼結体を製造可能な窒化ケイ素粉末を提供することを目的とする。本開示はまた、熱伝導性及び曲げ強度に優れる窒化ケイ素焼結体の製造方法を提供することを目的とする。 The present disclosure aims to provide a silicon nitride powder that can be used to produce sintered bodies with excellent thermal conductivity and bending strength. The present disclosure also aims to provide a method for producing silicon nitride sintered bodies with excellent thermal conductivity and bending strength.

本開示の一側面は、窒化ケイ素の一次粒子を含み、レーザー回折・散乱法によって測定される体積基準の粒子径の分布曲線において、小粒径からの積算値が全体の10%及び90%に達した時の粒子径を、それぞれD10及びD90としたときに、D90とD10との差が1.70μm以下である、窒化ケイ素粉末を提供する。 One aspect of the present disclosure provides a silicon nitride powder containing primary particles of silicon nitride, in which, in a volume-based particle size distribution curve measured by laser diffraction/scattering, the difference between D90 and D10 is 1.70 μm or less, when D10 and D90 are the particle sizes at which the cumulative values from small particle sizes reach 10% and 90% of the total, respectively.

上記窒化ケイ素粉末は、D90とD10との差(D90-D10)が所定値以下となることから、粒度分布が狭く、より緻密な組織を有する成形体(未焼成物)を調製することができる。上記成形体を焼成して得られる窒化ケイ素焼結体は、ボイドの発生等が抑制され、優れた熱伝導性及び曲げ強度を発揮し得る。 The above silicon nitride powder has a difference between D90 and D10 (D90 - D10) that is less than a specified value, making it possible to prepare a molded body (unsintered product) with a narrow particle size distribution and a denser structure. The silicon nitride sintered body obtained by sintering the above molded body has reduced void generation and can exhibit excellent thermal conductivity and bending strength.

上記窒化ケイ素粉末は、D90が2.00μm以下であってよい。D90の上限値を上記範囲内であると、粗大粒子の割合を十分に低減でき、焼結体の密度低下をより十分に抑制することができる。また、このような窒化ケイ素粉末は取扱い性により優れる。The silicon nitride powder may have a D90 of 2.00 μm or less. When the upper limit of D90 is within the above range, the proportion of coarse particles can be sufficiently reduced, and the decrease in density of the sintered body can be more sufficiently suppressed. Furthermore, such silicon nitride powder has excellent handleability.

上記窒化ケイ素粉末は、BET比表面積が8.0~15.0m/gであってよい。 The silicon nitride powder may have a BET specific surface area of 8.0 to 15.0 m 2 /g.

本開示の一側面は、上述の窒化ケイ素粉末を含む焼結原料を成形し焼成する工程を有する、窒化ケイ素焼結体の製造方法を提供する。 One aspect of the present disclosure provides a method for producing a silicon nitride sintered body, comprising the steps of molding and firing a sintering raw material containing the above-mentioned silicon nitride powder.

上記窒化ケイ素焼結体の製造方法は、上述の窒化ケイ素粉末を含む焼結原料を用いることから、得られる窒化ケイ素焼結体は、優れた熱伝導性及び曲げ強度を発揮し得る。 The above-mentioned method for manufacturing silicon nitride sintered bodies uses sintering raw materials containing the above-mentioned silicon nitride powder, and the resulting silicon nitride sintered bodies can exhibit excellent thermal conductivity and bending strength.

本開示によれば、熱伝導率及び曲げ強度に優れる焼結体を製造可能な窒化ケイ素粉末を提供できる。本開示によればまた、熱伝導性及び曲げ強度に優れる窒化ケイ素焼結体の製造方法を提供できる。 The present disclosure provides silicon nitride powder that can be used to produce sintered bodies with excellent thermal conductivity and bending strength.The present disclosure also provides a method for producing silicon nitride sintered bodies with excellent thermal conductivity and bending strength.

以下、本開示の実施形態について説明する。ただし、以下の実施形態は、本開示を説明するための例示であり、本開示を以下の内容に限定する趣旨ではない。 The following describes embodiments of the present disclosure. However, the following embodiments are examples for explaining the present disclosure and are not intended to limit the present disclosure to the following content.

本明細書において例示する材料は特に断らない限り、1種を単独で又は2種以上を組み合わせて用いることができる。組成物中の各成分の含有量は、組成物中の各成分に該当する物質が複数存在する場合には、特に断らない限り、組成物中に存在する当該複数の物質の合計量を意味する。本明細書における「工程」とは、互いに独立した工程であってもよく、同時に行われる工程であってもよい。Unless otherwise specified, the materials exemplified in this specification can be used singly or in combination of two or more. When multiple substances corresponding to each component are present in the composition, the content of each component in the composition means the total amount of those multiple substances present in the composition, unless otherwise specified. In this specification, the "steps" may be independent steps or steps performed simultaneously.

窒化ケイ素粉末の一実施形態は、窒化ケイ素の一次粒子を含み、レーザー回折・散乱法によって測定される体積基準の粒子径の分布曲線において、小粒径からの積算値が全体の10%及び90%に達した時の粒子径を、それぞれD10及びD90としたときに、D90とD10との差が1.70μm以下である。 One embodiment of the silicon nitride powder contains primary particles of silicon nitride, and in a volume-based particle size distribution curve measured by laser diffraction/scattering, when the particle sizes at which the cumulative values from small particle sizes reach 10% and 90% of the total are defined as D10 and D90, respectively, the difference between D90 and D10 is 1.70 μm or less.

上記D90とD10との差(D90-D10)の上限値は1.70μm以下であるが、例えば、1.65μm以下、1.60μm以下、1.55μm以下、1.50μm以下、又は1.45μm以下であってよい。上記差の上限値が上記範囲内であると、窒化ケイ素粉末を圧縮成形等して調製される成形体がより緻密な組織を有し得るため、焼結した際のボイドの発生等をより抑制することができる。つまり、得られる窒化ケイ素焼結体の熱伝導性及び曲げ強度をより高度に両立することができる。上記D90とD10との差の下限値は、例えば、0.50μm以上、0.80μm以上、又は1.00μm以上であってよい。上記差の下限値が上記範囲内であると、窒化ケイ素粉末が適度な粒度分布を有するため、一次粒子のパッキング密度をより向上させることができる。上記差は上述の範囲内で調整することができ、例えば、0.50~1.70μm、0.80~1.65μm、又は1.00~1.45μmであってよい。上記差は、窒化ケイ素粉末の製造時の粉砕条件等を調整することで制御できる。The upper limit of the difference between D90 and D10 (D90 - D10) is 1.70 μm or less, but may be, for example, 1.65 μm or less, 1.60 μm or less, 1.55 μm or less, 1.50 μm or less, or 1.45 μm or less. When the upper limit of the difference is within the above range, the molded body prepared by compression molding or the like of the silicon nitride powder can have a denser structure, thereby further suppressing the occurrence of voids during sintering. In other words, the resulting silicon nitride sintered body can achieve both high thermal conductivity and high bending strength. The lower limit of the difference between D90 and D10 may be, for example, 0.50 μm or more, 0.80 μm or more, or 1.00 μm or more. When the lower limit of the difference is within the above range, the silicon nitride powder has an appropriate particle size distribution, thereby further improving the packing density of the primary particles. The difference can be adjusted within the above range, for example, 0.50 to 1.70 μm, 0.80 to 1.65 μm, or 1.00 to 1.45 μm. The difference can be controlled by adjusting the grinding conditions during the production of the silicon nitride powder.

窒化ケイ素粉末のD90の上限値は、例えば、2.00μm以下、1.90μm以下、1.98μm以下、1.95μm以下、又は1.90μm以下であってよい。D90の上限値を上記範囲内であると、粗大粒子の割合を十分に低減でき、焼結体の密度低下をより十分に抑制することができる。D90の下限値は、例えば、1.40μm以上、1.50μm以上、1.52μm以上、1.55μm以上、1.60μm以上、又は1.65μm以上であってよい。D90は上述の範囲内で調整でき、例えば、1.40~2.00μm、又は1.50~1.90μmであってよい。窒化ケイ素粉末のD90は、例えば、窒化ケイ素粉末の製造時における粉砕条件等を調整することで制御できる。The upper limit of D90 of the silicon nitride powder may be, for example, 2.00 μm or less, 1.90 μm or less, 1.98 μm or less, 1.95 μm or less, or 1.90 μm or less. Keeping the upper limit of D90 within the above ranges allows for a sufficient reduction in the proportion of coarse particles, and more effectively suppresses a decrease in the density of the sintered body. The lower limit of D90 may be, for example, 1.40 μm or more, 1.50 μm or more, 1.52 μm or more, 1.55 μm or more, 1.60 μm or more, or 1.65 μm or more. D90 can be adjusted within the above range, for example, between 1.40 and 2.00 μm, or between 1.50 and 1.90 μm. The D90 of the silicon nitride powder can be controlled, for example, by adjusting the milling conditions during production of the silicon nitride powder.

窒化ケイ素粉末のD50の上限値は、例えば、0.75μm以下、又は0.72μm以下であってよい。D50の上限値が上記範囲内であると、窒化ケイ素焼結体の強度をより向上させることができる。窒化ケイ素粉末のD50の下限値は、例えば、0.50μm以上、又は0.55μm以上であってよい。窒化ケイ素粉末のD50は上述の範囲内で調整することができ、例えば、0.50~0.75μm、又は0.55~0.75μmであってよい。 The upper limit of D50 of the silicon nitride powder may be, for example, 0.75 μm or less, or 0.72 μm or less. When the upper limit of D50 is within the above range, the strength of the silicon nitride sintered body can be further improved. The lower limit of D50 of the silicon nitride powder may be, for example, 0.50 μm or more, or 0.55 μm or more. The D50 of the silicon nitride powder can be adjusted within the above range, and may be, for example, 0.50 to 0.75 μm, or 0.55 to 0.75 μm.

本明細書におけるD10、D50、及びD90はそれぞれ、レーザー回折・散乱法によって測定される体積基準の粒子径の分布曲線において、小粒径からの積算値が全体の10%、50%及び90%に達した時の粒子径をいう。レーザー解析散乱法は、JIS Z 8825:2013「粒子径解析-レーザー回折・散乱法」に記載の方法に準拠して測定できる。測定には、レーザー回折散乱法粒度分布測定装置(ベックマンコールター社製、商品名:LS-13 320)等を使用することができる。なお、D50は、メディアン径とも呼ばれ、窒化ケイ素粉末の平均粒径を意味する。 In this specification, D10, D50, and D90 refer to the particle sizes at which the cumulative value from the smallest particle size reaches 10%, 50%, and 90%, respectively, on the volume-based particle size distribution curve measured by laser diffraction/scattering. Laser diffraction/scattering measurements can be performed in accordance with the method described in JIS Z 8825:2013, "Particle Size Analysis - Laser Diffraction/Scattering Method." Measurements can be performed using a laser diffraction/scattering particle size distribution analyzer (manufactured by Beckman Coulter, Inc., product name: LS-13 320). D50, also known as the median diameter, refers to the average particle size of silicon nitride powder.

窒化ケイ素粉末のBET比表面積の下限値は、例えば、8.0m/g以上、8.5m/g以上、8.7m/g以上、又は9.0m/g以上であってよい。窒化ケイ素粉末のBET比表面積の上限値は、例えば、15.0m/g以下、13.0m/g以下、12.0m/g以下、11.0m/g以下、10.0m/g以下、9.5m/g以下、又は9.2m/g以下であってよい。窒化ケイ素粉末のBET比表面積は上述の範囲内で調整することができ、例えば、8.0~15.0m/g、又は8.5~13.0m/gであってよい。窒化ケイ素粉末のBET比表面積は、例えば、窒化ケイ素粉末の製造時における粉砕条件等を調整することで制御できる。 The lower limit of the BET specific surface area of the silicon nitride powder may be, for example, 8.0 m 2 /g or more, 8.5 m 2 /g or more, 8.7 m 2 /g or more, or 9.0 m 2 /g or more. The upper limit of the BET specific surface area of the silicon nitride powder may be, for example, 15.0 m 2 /g or less, 13.0 m 2 /g or less, 12.0 m 2 /g or less, 11.0 m 2 /g or less, 10.0 m 2 /g or less, 9.5 m 2 /g or less, or 9.2 m 2 /g or less. The BET specific surface area of the silicon nitride powder can be adjusted within the above-mentioned range and may be, for example, 8.0 to 15.0 m 2 /g, or 8.5 to 13.0 m 2 /g. The BET specific surface area of the silicon nitride powder can be controlled, for example, by adjusting the grinding conditions during the production of the silicon nitride powder.

本明細書におけるBET比表面積は、JIS Z 8830:2013「ガス吸着による粉体(固体)の比表面積測定方法」に記載の方法に準拠し、窒素ガスを使用してBET一点法によって測定される値である。 The BET specific surface area in this specification is a value measured by the BET single-point method using nitrogen gas in accordance with the method described in JIS Z 8830:2013 "Method for measuring the specific surface area of powders (solids) by gas adsorption."

窒化ケイ素の表面酸素量の上限値は、例えば、0.70質量%以下、0.60質量%以下、又は0.50質量%以下であってよい。窒化ケイ素の表面酸素量の上限値が上記範囲内であると、窒化ケイ素焼結体を製造した際の粒界相をより十分に低減することができ、熱伝導率をより向上させることができる。窒化ケイ素の表面酸素量の上限値が上記範囲内であるとまた、続く酸処理工程における酸処理時間を低減することができる。窒化ケイ素の表面酸素量の下限値は、例えば、0.20質量%以上、0.30質量%以上、0.35質量%以上、0.40質量%以上、又は0.45質量%以上であってよい。窒化ケイ素の表面酸素量の下限値が上記範囲内であると、窒化ケイ素を焼成させる際の粒成長を促進させることができ、窒化ケイ素焼結体の曲げ強度をより向上させることができる。窒化ケイ素の表面酸素量は上述の範囲で調整することができ、例えば、0.20~0.70質量%、又は0.20~0.50質量%であってよい。窒化ケイ素の表面酸素量は、例えば、窒化ケイ素粉末の製造における焼成工程における雰囲気の成分、並びに、焼成温度及び焼成時間等の調整によって制御できる。The upper limit of the surface oxygen content of silicon nitride may be, for example, 0.70% by mass or less, 0.60% by mass or less, or 0.50% by mass or less. When the upper limit of the surface oxygen content of silicon nitride is within the above range, the grain boundary phase can be more sufficiently reduced when producing a silicon nitride sintered body, thereby further improving thermal conductivity. When the upper limit of the surface oxygen content of silicon nitride is within the above range, the acid treatment time in the subsequent acid treatment step can also be reduced. The lower limit of the surface oxygen content of silicon nitride may be, for example, 0.20% by mass or more, 0.30% by mass or more, 0.35% by mass or more, 0.40% by mass or more, or 0.45% by mass or more. When the lower limit of the surface oxygen content of silicon nitride is within the above range, grain growth can be promoted during sintering of the silicon nitride, thereby further improving the bending strength of the silicon nitride sintered body. The surface oxygen content of silicon nitride can be adjusted within the above range, for example, 0.20 to 0.70% by mass or 0.20 to 0.50% by mass. The surface oxygen content of silicon nitride can be controlled, for example, by adjusting the composition of the atmosphere in the firing step in the production of silicon nitride powder, as well as the firing temperature, firing time, and the like.

本明細書における「表面酸素量」は以下の手順で求められる数値を意味する。窒化ケイ素粉末の酸素量及び窒素量は、酸素・窒素分析装置を用いて分析する。測定用の試料を、ヘリウムガスの雰囲気中、8℃/秒の昇温速度で20℃から2000℃まで昇温する。昇温に伴って脱離する酸素を赤外吸収法によって検知する。昇温当初は、窒化ケイ素粉末の表面に結合している酸素が脱離する。更に加熱し、温度が1400℃近傍に到達すると、窒化ケイ素が分解をし始める。窒化ケイ素の分解開始は、窒素が検出され始めることによって把握することができる。窒化ケイ素が分解をし始めると、窒化ケイ素粉末の内部にある酸素が脱離する。したがって、この段階で脱離する酸素は、内部酸素量に相当するため、窒素が検出される前までに検出され、定量された酸素量を表面酸素量とする。In this specification, "surface oxygen content" refers to a value determined by the following procedure. The oxygen and nitrogen content of silicon nitride powder is analyzed using an oxygen/nitrogen analyzer. The measurement sample is heated from 20°C to 2000°C at a heating rate of 8°C/sec in a helium gas atmosphere. The oxygen released as the temperature rises is detected using infrared absorption. Initially, oxygen bonded to the surface of the silicon nitride powder is released. With further heating, when the temperature reaches approximately 1400°C, the silicon nitride begins to decompose. The start of silicon nitride decomposition can be determined by the start of nitrogen detection. When silicon nitride begins to decompose, oxygen inside the silicon nitride powder is released. Therefore, the oxygen released at this stage corresponds to the internal oxygen content, and the amount of oxygen detected and quantified before nitrogen is detected is considered to be the surface oxygen content.

上述の窒化ケイ素粉末は、例えば、以下のような方法で製造することができる。窒化ケイ素粉末の製造方法の一実施形態は、ケイ素粉末を、窒素と、水素及びアンモニアからなる群より選択される少なくとも一種とを含む雰囲気下で焼成して焼成物を得る工程(以下、焼成工程ともいう)と、上記焼成物を湿式粉砕して粉砕物を得る工程(以下、粉砕工程ともいう)と、上記粉砕物を酸で処理し酸処理物を得る工程(以下、酸処理工程ともいう)と、上記酸処理物を湿式分級する工程(以下、分級工程ともいう)と、を有する。The silicon nitride powder described above can be produced, for example, by the following method. One embodiment of a method for producing silicon nitride powder includes the steps of: calcining silicon powder in an atmosphere containing nitrogen and at least one gas selected from the group consisting of hydrogen and ammonia to obtain a calcined product (hereinafter also referred to as the calcining step); wet-pulverizing the calcined product to obtain a pulverized product (hereinafter also referred to as the pulverization step); treating the pulverized product with acid to obtain an acid-treated product (hereinafter also referred to as the acid-treatment step); and wet-classifying the acid-treated product (hereinafter also referred to as the classification step).

ケイ素粉末としては、酸素濃度の低いケイ素粉末を用いてもよい。ケイ素粉末の酸素濃度の上限値は、例えば、0.40質量%以下、0.30質量%以下、又は0.20質量%以下であってよい。ケイ素粉末の酸素濃度を上記範囲内とすることで、得られる窒化ケイ素粉末の内部における酸素量をより低減できる。ケイ素粉末の酸素濃度の下限値は、例えば、0.10質量%以上、又は0.15質量%以上であってよい。ケイ素粉末の酸素濃度は上述の範囲で調整することができ、例えば、0.10~0.40質量%であってよい。 Silicon powder with a low oxygen concentration may be used. The upper limit of the oxygen concentration of the silicon powder may be, for example, 0.40% by mass or less, 0.30% by mass or less, or 0.20% by mass or less. By keeping the oxygen concentration of the silicon powder within the above range, the amount of oxygen inside the resulting silicon nitride powder can be further reduced. The lower limit of the oxygen concentration of the silicon powder may be, for example, 0.10% by mass or more, or 0.15% by mass or more. The oxygen concentration of the silicon powder can be adjusted within the above range and may be, for example, 0.10 to 0.40% by mass.

本明細書におけるケイ素粉末の酸素濃度は、赤外線吸収法によって測定される値を意味する。 The oxygen concentration of silicon powder in this specification refers to the value measured by infrared absorption method.

ケイ素粉末は、市販の物を用いることもでき、別途調製したものを用いてもよい。ケイ素粉末の酸素濃度が高い場合には、例えば、フッ化水素酸を含む前処理液を用いて、ケイ素粉末に結合する酸素量を低減することができる。例えば、上記窒化ケイ素粉末の製造方法は、フッ化水素酸を含む前処理液を用いてケイ素粉末を前処理し、酸素濃度が0.40質量%以上であるケイ素粉末を得る前処理工程を更に有していてもよい。 Commercially available silicon powder can be used, or separately prepared silicon powder can be used. If the silicon powder has a high oxygen concentration, the amount of oxygen bound to the silicon powder can be reduced, for example, by using a pretreatment liquid containing hydrofluoric acid. For example, the above-mentioned method for producing silicon nitride powder may further include a pretreatment step in which silicon powder is pretreated with a pretreatment liquid containing hydrofluoric acid to obtain silicon powder with an oxygen concentration of 0.40% by mass or more.

前処理液は、フッ化水素酸を含むが、例えば、塩酸等の酸との混酸であってもよく、フッ化水素酸のみからなってもよい。前処理工程における前処理液の温度は、例えば、40~80℃であってよい。また、前処理液とケイ素粉末とを接触させる時間は、例えば、1~10時間であってよい。The pretreatment liquid contains hydrofluoric acid, but may be a mixed acid with an acid such as hydrochloric acid, or may consist solely of hydrofluoric acid. The temperature of the pretreatment liquid in the pretreatment step may be, for example, 40 to 80°C. The time for which the pretreatment liquid is in contact with the silicon powder may be, for example, 1 to 10 hours.

焼成工程では、ケイ素粉末を、窒素と、水素及びアンモニアからなる群より選択される少なくも一種と、を含む混合雰囲気下で焼成して窒化ケイ素を含む焼成物を得る。混合雰囲気における水素及びアンモニアの合計の含有量は、混合雰囲気全体を基準として、例えば、10~40体積%であってよい。焼成温度は、例えば、1100~1450℃、又は1200~1400℃であってよい。焼成時間は、例えば、30~100時間であってよい。In the firing step, the silicon powder is fired in a mixed atmosphere containing nitrogen and at least one gas selected from the group consisting of hydrogen and ammonia to obtain a fired product containing silicon nitride. The total content of hydrogen and ammonia in the mixed atmosphere may be, for example, 10 to 40 volume % based on the entire mixed atmosphere. The firing temperature may be, for example, 1100 to 1450°C, or 1200 to 1400°C. The firing time may be, for example, 30 to 100 hours.

粉砕工程では、焼成工程で得られた上記焼成物を湿式で粉砕して粉砕物を得る。焼成物を粉砕し、粒度を調整することによって、後の酸処理工程における酸による表面処理の制御が容易となり、窒化ケイ素の一次粒子における表面酸素量の制御が容易なものとなる。焼成工程で得られる窒化ケイ素を含む焼成物が、塊状、インゴット状等になっている場合、粉砕工程を行う効果がより顕著である。In the pulverization process, the sintered product obtained in the sintering process is wet-pulverized to obtain a pulverized product. By pulverizing the sintered product and adjusting the particle size, it becomes easier to control the surface treatment with acid in the subsequent acid treatment process, and it becomes easier to control the amount of surface oxygen in the primary particles of silicon nitride. The effect of performing the pulverization process is more pronounced when the sintered product containing silicon nitride obtained in the sintering process is in the form of a block, ingot, etc.

粉砕は、粗粉砕と微粉砕というように複数段階に分けて行ってもよい。粉砕工程は、例えば、乾式粉砕工程を含んでもよい。その場合、粉砕工程は、乾式粉砕の後、湿式粉砕を行う工程であってよい。湿式粉砕に使用される媒体は、例えば、水等であってよい。 The grinding process may be carried out in multiple stages, such as coarse grinding and fine grinding. The grinding process may include, for example, a dry grinding process. In this case, the grinding process may be a process in which wet grinding is carried out after dry grinding. The medium used for wet grinding may be, for example, water.

粉砕には、例えば、ボールミル等を用いることができる。ボールミルを使用する場合、容器へのボールの充填率は、目的とする窒化ケイ素粉末の粒度分布に合わせて調整することができる。容器へのボールの充填率の下限値は、容器の容積を基準として、例えば、40体積%以上、45体積%以上、50体積%以上、又は60体積%以上であってよい。容器へのボールの充填率の上限値は、容器の容積を基準として、例えば、70体積%以下、又は65体積%以下であってよい。 For example, a ball mill or the like can be used for pulverization. When using a ball mill, the ball filling rate in the container can be adjusted to match the particle size distribution of the desired silicon nitride powder. The lower limit of the ball filling rate in the container, based on the volume of the container, may be, for example, 40 vol.% or more, 45 vol.% or more, 50 vol.% or more, or 60 vol.% or more. The upper limit of the ball filling rate in the container, based on the volume of the container, may be, for example, 70 vol.% or less, or 65 vol.% or less.

粉砕工程における粉砕処理の時間(粉砕時間)の下限値は、例えば、5時間以上、6時間以上、7時間以上、又は8時間以上であってよい。粉砕時間の下限値を上記範囲内とすることで、粉砕物を十分に細かくすることができ、酸処理工程での酸処理効率をより向上させることができる。上記粉砕処理の時間の上限値は、例えば、15時間以下、14時間以下、13時間以下、又は12時間以下であってよい。粉砕時間の上限値を上記範囲内とすることで、焼成物を十分に粉砕することができ、過剰な粉砕を防ぐこともできる。粉砕時間は上述の範囲内で調整してよく、例えば、5~15時間、又は8~12時間であってよい。 The lower limit of the grinding time (grinding time) in the grinding step may be, for example, 5 hours or more, 6 hours or more, 7 hours or more, or 8 hours or more. By setting the lower limit of the grinding time within the above range, the ground material can be sufficiently finely ground, and the acid treatment efficiency in the acid treatment step can be further improved. The upper limit of the grinding time may be, for example, 15 hours or less, 14 hours or less, 13 hours or less, or 12 hours or less. By setting the upper limit of the grinding time within the above range, the fired material can be sufficiently ground and excessive grinding can be prevented. The grinding time may be adjusted within the above range, and may be, for example, 5 to 15 hours or 8 to 12 hours.

酸処理工程では、粉砕物を酸と接触させて処理し酸処理物を得る。酸としては、例えば、フッ化水素、及び塩化水素等が挙げられる。酸は、フッ化水素と塩化水素との混酸であってもよく、フッ化水素又は塩化水素のいずれか単独であってもよいが、好ましくはフッ化水素を含む。酸は、水溶液(例えば、フッ化水素酸又は塩酸)であってよい。In the acid treatment step, the ground material is brought into contact with an acid to obtain an acid-treated product. Examples of acids include hydrogen fluoride and hydrogen chloride. The acid may be a mixed acid of hydrogen fluoride and hydrogen chloride, or may be either hydrogen fluoride or hydrogen chloride alone, but preferably contains hydrogen fluoride. The acid may be an aqueous solution (e.g., hydrofluoric acid or hydrochloric acid).

酸(例えば、フッ化水素酸)の濃度の上限値は、例えば、55質量%以下、40質量%以下、38質量%以下、35質量%以下、又は30質量%以下であってよい。酸の濃度の下限値は、例えば、10質量%以上、11質量%以上、又は12質量%以上であってよい。酸の濃度の下限値を上記範囲内とすることで、酸処理不足を防ぐことができる。酸の濃度は上述の範囲内で調整してよく、例えば、10~55質量%、11~38質量%、又は12~30質量%であってよい。 The upper limit of the acid (e.g., hydrofluoric acid) concentration may be, for example, 55% by mass or less, 40% by mass or less, 38% by mass or less, 35% by mass or less, or 30% by mass or less. The lower limit of the acid concentration may be, for example, 10% by mass or more, 11% by mass or more, or 12% by mass or more. By setting the lower limit of the acid concentration within the above range, insufficient acid treatment can be prevented. The acid concentration may be adjusted within the above range, and may be, for example, 10 to 55% by mass, 11 to 38% by mass, or 12 to 30% by mass.

粉砕物と酸との接触の手段は、例えば、酸中に粉砕物を分散させる方法であってよい。 The means for contacting the ground material with the acid may be, for example, a method of dispersing the ground material in the acid.

酸処理工程における酸(例えば、水溶液)の温度の下限値は、例えば、40℃以上、45℃以上、50℃以上、又は60℃以上であってよい。酸処理工程における酸の温度の上限値は、80℃以下、75℃以下、又は70℃以下であってよい。酸処理工程における酸の温度は上述の範囲内で調整してよく、例えば、40~80℃、45~75℃、又は50~70℃であってよい。 The lower limit of the temperature of the acid (e.g., aqueous solution) in the acid treatment step may be, for example, 40°C or higher, 45°C or higher, 50°C or higher, or 60°C or higher. The upper limit of the temperature of the acid in the acid treatment step may be 80°C or lower, 75°C or lower, or 70°C or lower. The temperature of the acid in the acid treatment step may be adjusted within the above-mentioned range, and may be, for example, 40 to 80°C, 45 to 75°C, or 50 to 70°C.

酸処理工程において、焼成物又は焼成物を粉砕して得られる粉砕物と酸と接触させる時間(酸処理時間)の下限値は、例えば、1.0時間以上、1.2時間以上、1.5時間以上、又は2.0時間以上であってよい。酸処理時間の下限値を上記範囲内とすることで、酸処理不足を防ぐことができる。上記酸処理時間は、例えば、10.0時間以下、9.7時間以下、9.5時間以下、9.0時間以下、8.5時間以下、又は8.0時間以下であってよい。上記酸処理時間は上述の範囲内で調整してよく、例えば、1.0~10.0時間、1.2~9.7時間、又は2.0~8.0時間であってよい。In the acid treatment step, the lower limit of the time (acid treatment time) for contacting the calcined product or the pulverized product obtained by pulverizing the calcined product with acid may be, for example, 1.0 hour or more, 1.2 hours or more, 1.5 hours or more, or 2.0 hours or more. By setting the lower limit of the acid treatment time within the above range, insufficient acid treatment can be prevented. The acid treatment time may be, for example, 10.0 hours or less, 9.7 hours or less, 9.5 hours or less, 9.0 hours or less, 8.5 hours or less, or 8.0 hours or less. The acid treatment time may be adjusted within the above range, and may be, for example, 1.0 to 10.0 hours, 1.2 to 9.7 hours, or 2.0 to 8.0 hours.

分級工程では、粉砕工程及び酸処理工程を経て調製された上記酸処理物を更に湿式で分級して、所望の粒度分布を有する窒化ケイ素粉末を調製する。例えば、粗粉を除去して窒化ケイ素粉末のD90を調整する等することができる。湿式分級は、例えば、遠心分離等によって行うことができる。遠心分離機は、例えば、液体サイクロン(株式会社村田製作所製、商品名:3液分級サイクロン TR-10型)等を用いることができる。入口に印加する圧力(入口圧力)は、例えば、0.2~1.0MPa、又は0.3~0.7MPaであってよい。 In the classification process, the acid-treated product prepared through the pulverization and acid treatment processes is further wet-classified to produce silicon nitride powder with the desired particle size distribution. For example, coarse particles can be removed to adjust the D90 of the silicon nitride powder. Wet classification can be performed, for example, by centrifugation. The centrifuge can be, for example, a liquid cyclone (manufactured by Murata Manufacturing Co., Ltd., product name: Three-liquid Classifying Cyclone TR-10). The pressure applied to the inlet (inlet pressure) can be, for example, 0.2 to 1.0 MPa, or 0.3 to 0.7 MPa.

上述の製造方法によって得られる窒化ケイ素粉末は焼結性に優れる。すなわち、上述の窒化ケイ素粉末は焼結体原料に好適に用いることができる。 The silicon nitride powder obtained by the above-mentioned manufacturing method has excellent sinterability. In other words, the above-mentioned silicon nitride powder can be suitably used as a raw material for sintered bodies.

窒化ケイ素焼結体の製造方法の一実施形態は、上述の窒化ケイ素粉末を含む焼結原料を成形し焼成する工程を有する。 One embodiment of a method for producing a silicon nitride sintered body includes molding and firing a sintering raw material containing the above-mentioned silicon nitride powder.

焼結原料は窒化ケイ素粉末の他に、酸化物系焼結助剤を含んでいてもよい。酸化物系焼結助剤としては、例えば、Y3、MgO及びAl等が挙げられる。焼結原料における酸化物系焼結助剤の含有量は、例えば、3~10質量%であってよい。 The sintering raw material may contain an oxide-based sintering aid in addition to the silicon nitride powder. Examples of the oxide-based sintering aid include Y 2 O 3, MgO, and Al 2 O 3. The content of the oxide-based sintering aid in the sintering raw material may be, for example, 3 to 10 mass %.

上記工程では、上述の焼結原料を、例えば3.0~30.0MPaの成形圧力で加圧して成形体を得る。成形体は一軸加圧して作製してもよいし、CIPによって作製してもよい。また、ホットプレスによって成形しながら焼成してもよい。成形体の焼成は、窒素ガス又はアルゴンガス等の不活性ガス雰囲気中で行ってよい。焼成時の圧力は、0.7~1.0MPaであってよい。焼成温度は1860~2100℃であってよく、1880~2000℃であってもよい。当該焼成温度における焼成時間は6~20時間であってよく、8~16時間であってよい。焼成温度までの昇温速度は、例えば1.0~10.0℃/時間であってよい。In the above process, the above-mentioned sintering raw materials are pressed at a molding pressure of, for example, 3.0 to 30.0 MPa to obtain a molded body. The molded body may be produced by uniaxial pressing or by CIP. It may also be fired while being molded by hot pressing. The molded body may be fired in an inert gas atmosphere such as nitrogen gas or argon gas. The pressure during firing may be 0.7 to 1.0 MPa. The firing temperature may be 1860 to 2100°C, or 1880 to 2000°C. The firing time at this firing temperature may be 6 to 20 hours, or 8 to 16 hours. The rate of temperature rise to the firing temperature may be, for example, 1.0 to 10.0°C/hour.

得られる窒化ケイ素焼結体は、粒界相が低減されており、緻密な組織を有することから、優れた熱伝導率及び曲げ強度を発揮し得る。 The resulting silicon nitride sintered body has a reduced grain boundary phase and a dense structure, which allows it to exhibit excellent thermal conductivity and bending strength.

窒化ケイ素焼結体の熱伝導率は、25℃の環境下において、例えば、90W/(m・K)以上、95W/(m・K)以上、100W/(m・K)以上、又は105W/(m・K)以上、又は110W/(m・K)以上とすることができる。本明細書における窒化ケイ素焼結体の熱伝導率は、レーザーフラッシュ法(JIS R1611に準拠)によって熱拡散率と比熱容量を測定し、焼結体の密度、熱拡散率及び比熱容量の積を算出して得られる値を意味する。 The thermal conductivity of silicon nitride sintered bodies can be, for example, 90 W/(m·K) or more, 95 W/(m·K) or more, 100 W/(m·K) or more, 105 W/(m·K) or more, or 110 W/(m·K) or more in an environment of 25°C. The thermal conductivity of silicon nitride sintered bodies in this specification refers to the value obtained by measuring the thermal diffusivity and specific heat capacity using the laser flash method (in accordance with JIS R1611) and calculating the product of the density, thermal diffusivity, and specific heat capacity of the sintered body.

窒化ケイ素焼結体の曲げ強度は、室温で、例えば、550MPa以上、600MPa以上、又は650MPa以上とすることができる。本明細書における窒化ケイ素焼結体の曲げ強度は、JIS R1601:2008に準じて強度測定用の試験片を作製し、室温において測定される3点曲げ強さを意味する。 The bending strength of the silicon nitride sintered body can be, for example, 550 MPa or more, 600 MPa or more, or 650 MPa or more at room temperature. In this specification, the bending strength of the silicon nitride sintered body refers to the three-point bending strength measured at room temperature using a test piece for strength measurement prepared in accordance with JIS R1601:2008.

以上、幾つかの実施形態について説明したが、本開示は上記実施形態に何ら限定されるものではない。また、上述した実施形態についての説明内容は、互いに適用することができる。 Although several embodiments have been described above, the present disclosure is in no way limited to the above-described embodiments. Furthermore, the descriptions of the above-described embodiments can be applied to each other.

以下、実施例及び比較例を参照して本開示の内容をより詳細に説明する。ただし、本開示は、下記の実施例に限定されるものではない。 The present disclosure will be explained in more detail below with reference to examples and comparative examples. However, the present disclosure is not limited to the following examples.

(実施例1)
<窒化ケイ素粉末の調製>
市販のケイ素粉末(比表面積:3.0m/g)を、60℃に温度調整した、塩化水素及びフッ化水素を含む混酸中に浸漬して、60℃に維持し、2時間、前処理を施した。上記混酸は、市販の塩酸(濃度:35質量%)とフッ化水素酸(濃度:55質量%)とを、10:1の質量比で混合したものを用いた。その後、混酸からケイ素粉末を取り出して水で洗浄し、窒素雰囲気下で乾燥した。乾燥後のケイ素粉末の酸素濃度は、0.4質量%であった。この酸素濃度は、赤外線吸収法によって測定した。
Example 1
<Preparation of silicon nitride powder>
Commercially available silicon powder (specific surface area: 3.0 m 2 /g) was immersed in a mixed acid containing hydrogen chloride and hydrogen fluoride, the temperature of which was adjusted to 60°C, and the mixture was maintained at 60°C for 2 hours for pretreatment. The mixed acid used was a mixture of commercially available hydrochloric acid (concentration: 35% by mass) and hydrofluoric acid (concentration: 55% by mass) in a mass ratio of 10:1. The silicon powder was then removed from the mixed acid, washed with water, and dried under a nitrogen atmosphere. The oxygen concentration of the dried silicon powder was 0.4% by mass. This oxygen concentration was measured by infrared absorption.

乾燥後のケイ素粉末を用いて成形体(嵩密度:1.4g/cm)を作製した。得られた成形体を電気炉内に静置し、1400℃で60時間かけて焼成し窒化ケイ素を含む焼成体を作製した。焼成時の雰囲気として、窒素と水素との混合ガス(NとHとを標準状態における体積比で80:20となるように混合した混合ガス)を供給した。得られた焼成体を粗粉砕した後、ボールミルで湿式粉砕した。湿式粉砕は、容器に対するボールの充填率を60体積%とし、溶媒として水を用い、粉砕時間を8時間とした。 A molded body (bulk density: 1.4 g/cm 3 ) was produced using the dried silicon powder. The obtained molded body was placed in an electric furnace and fired at 1400°C for 60 hours to produce a fired body containing silicon nitride. A mixed gas of nitrogen and hydrogen (a mixed gas in which N 2 and H 2 were mixed at a volume ratio of 80:20 under standard conditions) was supplied as the firing atmosphere. The obtained fired body was coarsely crushed and then wet-pulverized in a ball mill. For the wet crushing, the ball filling rate to the container was 60% by volume, water was used as the solvent, and the crushing time was 8 hours.

湿式粉砕して得られた窒化ケイ素粉末を、温度60℃のフッ化水素酸(フッ化水素酸濃度:15質量%)中に2時間浸漬して酸処理した。その後、フッ化水素酸から窒化ケイ素粉末を取り出して水で洗浄した。さらに、窒化ケイ素粉末に水を加え、0.5MPaの条件で、湿式分級をし、上澄みを除去したものを、窒素雰囲気下で乾燥した。こうして窒化ケイ素粉末を得た。The silicon nitride powder obtained by wet milling was immersed in hydrofluoric acid (hydrofluoric acid concentration: 15% by mass) at 60°C for 2 hours for acid treatment. The silicon nitride powder was then removed from the hydrofluoric acid and washed with water. Water was then added to the silicon nitride powder, and the mixture was wet classified at 0.5 MPa. The supernatant was removed and dried under a nitrogen atmosphere. This yielded silicon nitride powder.

<窒化ケイ素粉末の評価:D10、D50、及びD90の測定>
窒化ケイ素粉末のD10、D50、及びD90を、JIS Z 8825:2013「粒子径解析-レーザー回折・散乱法」に記載の方法に準拠してレーザー解析散乱法で測定した。測定には、レーザー回折散乱法粒度分布測定装置(ベックマンコールター社製、商品名:LS-13 320)を用いた。
<Evaluation of Silicon Nitride Powder: Measurement of D10, D50, and D90>
The D10, D50, and D90 of the silicon nitride powder were measured by a laser diffraction scattering method in accordance with the method described in JIS Z 8825:2013 "Particle size analysis - laser diffraction and scattering method." For the measurements, a laser diffraction scattering particle size distribution analyzer (manufactured by Beckman Coulter, Inc., product name: LS-13 320) was used.

<窒化ケイ素粉末の評価:BET比表面積の測定>
BET比表面積は、JIS Z 8803:2013に準拠し、窒素ガスを使用してBET一点法によって測定した。結果を表1に示す。
<Evaluation of Silicon Nitride Powder: Measurement of BET Specific Surface Area>
The BET specific surface area was measured by the BET single-point method using nitrogen gas in accordance with JIS Z 8803:2013. The results are shown in Table 1.

<窒化ケイ素粉末の評価:表面酸素量の測定>
表面酸素量は、酸素/窒素同時分析装置(堀場製作所社製、装置名:EMGA-920)を用いて測定した。具体的には、窒化ケイ素粉末を、ヘリウム雰囲気中、昇温速度8℃/秒で20℃から2000℃まで加熱し、窒素が検出される前までの酸素量を定量することで測定した。
<Evaluation of Silicon Nitride Powder: Measurement of Surface Oxygen Amount>
The surface oxygen content was measured using an oxygen/nitrogen simultaneous analyzer (manufactured by Horiba, Ltd., model EMGA-920). Specifically, the silicon nitride powder was heated in a helium atmosphere from 20°C to 2000°C at a temperature increase rate of 8°C/sec, and the amount of oxygen was measured before nitrogen was detected.

[窒化ケイ素焼結体の製造]
容器に、調製した窒化ケイ素粉末を90質量部、平均粒径が1.5μmであるY粉末を5質量部、及び、平均粒径が1.2μmであるYb粉末を5質量部、測り取り、メタノールを加えて、4時間湿式混合した。その後、乾燥して得た混合粉末(焼成原料)を10MPaの圧力で金型成形し、その後、更に25MPaの圧力で冷間等方圧加圧(CIP)成形した。得られた成形体を、窒化ケイ素粉末及びBN粉末の混合粉末からなる詰め粉とともにカーボン製坩堝にセットし、1MPaの窒素加圧雰囲気下、温度1900℃で12時間焼成して窒化ケイ素焼結体を製造した。
[Production of silicon nitride sintered body]
90 parts by mass of the prepared silicon nitride powder, 5 parts by mass of Y2O3 powder with an average particle size of 1.5 μm, and 5 parts by mass of Yb2O3 powder with an average particle size of 1.2 μm were weighed into a container, and methanol was added and wet-mixed for 4 hours. The dried mixed powder (sintered raw material) was then molded in a mold at a pressure of 10 MPa and then cold isostatically pressed (CIP) at a pressure of 25 MPa. The resulting molded body was placed in a carbon crucible together with a packed powder consisting of a mixed powder of silicon nitride powder and BN powder, and sintered at a temperature of 1900 °C for 12 hours under a nitrogen pressure of 1 MPa to produce a silicon nitride sintered body.

<窒化ケイ素焼結体の熱伝導率測定>
窒化ケイ素焼結体を研削加工して、熱伝導率測定用の10mmφ×3mmの円盤体を作製した。レーザーフラッシュ法(JIS R1611に準拠)により熱拡散率と比熱容量を測定し、焼結体の密度、熱拡散率及び比熱容量の積を算出して、室温における熱伝導率とした。結果を表1に示す。なお、表1において熱伝導率の測定結果は、後述する比較例1で調製した窒化ケイ素焼結体を基準とした相対値で示した。
<Measurement of thermal conductivity of sintered silicon nitride>
The silicon nitride sintered body was ground to prepare a 10 mm diameter x 3 mm disk for measuring thermal conductivity. Thermal diffusivity and specific heat capacity were measured using the laser flash method (based on JIS R1611), and the product of the density, thermal diffusivity, and specific heat capacity of the sintered body was calculated to determine the thermal conductivity at room temperature. The results are shown in Table 1. The thermal conductivity measurement results in Table 1 are shown as relative values based on the silicon nitride sintered body prepared in Comparative Example 1, which will be described later.

<窒化ケイ素焼結体の曲げ強度測定>
窒化ケイ素焼結体から、JIS R1601:2008に準じて強度測定用の試験片を作製し、室温における3点曲げ強さを測定した。結果を表1に示す。なお、表1において曲げ強度の測定結果は、後述する比較例1で調製した窒化ケイ素焼結体を基準とした相対値で示した。
<Measurement of bending strength of sintered silicon nitride>
Test pieces for strength measurement were prepared from the silicon nitride sintered body in accordance with JIS R1601:2008, and the three-point bending strength was measured at room temperature. The results are shown in Table 1. Note that the bending strength measurement results in Table 1 are shown as relative values based on the silicon nitride sintered body prepared in Comparative Example 1, which will be described later.

<窒化ケイ素焼結体の評価>
窒化ケイ素焼結体について、下記の基準で評価を行った。
A:熱伝導率(相対値)が1.20以上、且つ曲げ強度(相対値)が1.10以上である。
B:熱伝導率(相対値)が1.20以上、且つ曲げ強度(相対値)が1.05以上1.10未満である、又は、熱伝導率(相対値)が1.10以上1.20未満、且つ曲げ強度(相対値)が1.10以上である。
C:熱伝導率(相対値)が1.10以上1.20未満、且つ曲げ強度(相対値)が1.05以上1.10未満である。
D:熱伝導率(相対値)が1.10未満、又は曲げ強度(相対値)が1.05未満である。
<Evaluation of silicon nitride sintered body>
The silicon nitride sintered body was evaluated according to the following criteria.
A: Thermal conductivity (relative value) is 1.20 or more, and bending strength (relative value) is 1.10 or more.
B: Thermal conductivity (relative value) is 1.20 or more, and bending strength (relative value) is 1.05 or more and less than 1.10, or thermal conductivity (relative value) is 1.10 or more and less than 1.20, and bending strength (relative value) is 1.10 or more.
C: Thermal conductivity (relative value) is 1.10 or more and less than 1.20, and bending strength (relative value) is 1.05 or more and less than 1.10.
D: Thermal conductivity (relative value) is less than 1.10, or bending strength (relative value) is less than 1.05.

(実施例2)
湿式分級の条件を表1に記載した条件にしたこと以外は、実施例1と同様にして、窒化ケイ素粉末を調製した。得られた窒化ケイ素粉末について、実施例1と同様に評価を行った。結果を表1に示す。
Example 2
Silicon nitride powder was prepared in the same manner as in Example 1, except that the wet classification conditions were as shown in Table 1. The obtained silicon nitride powder was evaluated in the same manner as in Example 1. The results are shown in Table 1.

(実施例3)
湿式粉砕の条件を表1に記載した条件にしたこと以外は、実施例1と同様にして、窒化ケイ素粉末を調製した。得られた窒化ケイ素粉末について、実施例1と同様に評価を行った。結果を表1に示す。
Example 3
Silicon nitride powder was prepared in the same manner as in Example 1, except that the wet-pulverization conditions were as shown in Table 1. The obtained silicon nitride powder was evaluated in the same manner as in Example 1. The results are shown in Table 1.

(比較例1)
湿式分級の条件を表1に記載した条件にしたこと以外は、実施例1と同様にして、窒化ケイ素粉末を調製した。得られた窒化ケイ素粉末について、実施例1と同様に評価を行った。結果を表1に示す。
(Comparative Example 1)
Silicon nitride powder was prepared in the same manner as in Example 1, except that the wet classification conditions were as shown in Table 1. The obtained silicon nitride powder was evaluated in the same manner as in Example 1. The results are shown in Table 1.

本開示によれば、熱伝導率及び曲げ強度に優れる焼結体を製造可能な窒化ケイ素粉末を提供できる。本開示によればまた、熱伝導性及び曲げ強度に優れる窒化ケイ素焼結体の製造方法を提供できる。 The present disclosure provides silicon nitride powder that can be used to produce sintered bodies with excellent thermal conductivity and bending strength.The present disclosure also provides a method for producing silicon nitride sintered bodies with excellent thermal conductivity and bending strength.

Claims (3)

窒化ケイ素の一次粒子を含み、
BET比表面積が8.0~15.0m/gであり、
表面酸素量が0.30~0.70質量%であり、
レーザー回折・散乱法によって測定される体積基準の粒子径の分布曲線において、小粒径からの積算値が全体の10%及び90%に達した時の粒子径を、それぞれD10及びD90としたときに、D90とD10との差が1.52μm以上1.70μm以下である、焼結体原料用窒化ケイ素粉末。
Contains primary particles of silicon nitride,
The BET specific surface area is 8.0 to 15.0 m 2 /g;
The surface oxygen content is 0.30 to 0.70 mass %,
A silicon nitride powder for use as a raw material for sintered bodies, in which, in a volume-based particle size distribution curve measured by a laser diffraction /scattering method, the particle sizes at which the integrated values from small particle sizes reach 10% and 90% of the total are defined as D10 and D90, respectively, and the difference between D90 and D10 is 1.52 μm or more and 1.70 μm or less.
D90が2.00μm以下である、請求項1に記載の焼結体原料用窒化ケイ素粉末。 2. The silicon nitride powder for use as a raw material for a sintered body according to claim 1, wherein D90 is 2.00 μm or less. 請求項1又は2に記載の焼結体原料用窒化ケイ素粉末を含む焼結原料を成形し焼成する工程を有する、窒化ケイ素焼結体の製造方法。 A method for producing a silicon nitride sintered body, comprising the steps of molding and firing a sintering raw material containing the silicon nitride powder for a sintered body raw material according to claim 1 or 2.
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