JP7620545B2 - Silicon nitride powder and its manufacturing method, and method for manufacturing sintered silicon nitride - Google Patents
Silicon nitride powder and its manufacturing method, and method for manufacturing sintered silicon nitride Download PDFInfo
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- 229910052581 Si3N4 Inorganic materials 0.000 title claims description 190
- HQVNEWCFYHHQES-UHFFFAOYSA-N silicon nitride Chemical compound N12[Si]34N5[Si]62N3[Si]51N64 HQVNEWCFYHHQES-UHFFFAOYSA-N 0.000 title claims description 190
- 239000000843 powder Substances 0.000 title claims description 162
- 238000004519 manufacturing process Methods 0.000 title claims description 50
- 238000000034 method Methods 0.000 title claims description 21
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 37
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 claims description 30
- PXGOKWXKJXAPGV-UHFFFAOYSA-N Fluorine Chemical compound FF PXGOKWXKJXAPGV-UHFFFAOYSA-N 0.000 claims description 30
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 30
- 239000000460 chlorine Substances 0.000 claims description 30
- 229910052801 chlorine Inorganic materials 0.000 claims description 30
- 239000011737 fluorine Substances 0.000 claims description 30
- 229910052731 fluorine Inorganic materials 0.000 claims description 30
- 239000001301 oxygen Substances 0.000 claims description 30
- 229910052760 oxygen Inorganic materials 0.000 claims description 30
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 27
- 238000005245 sintering Methods 0.000 claims description 23
- 238000010304 firing Methods 0.000 claims description 20
- 239000002245 particle Substances 0.000 claims description 16
- 239000002994 raw material Substances 0.000 claims description 15
- 239000000377 silicon dioxide Substances 0.000 claims description 15
- 239000011164 primary particle Substances 0.000 claims description 10
- 229910052799 carbon Inorganic materials 0.000 claims description 8
- 239000012299 nitrogen atmosphere Substances 0.000 claims description 8
- 239000013078 crystal Substances 0.000 claims description 6
- 238000006243 chemical reaction Methods 0.000 description 19
- 239000012535 impurity Substances 0.000 description 16
- 230000000052 comparative effect Effects 0.000 description 8
- 239000007789 gas Substances 0.000 description 7
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 6
- 239000006230 acetylene black Substances 0.000 description 6
- 238000013329 compounding Methods 0.000 description 6
- 239000005350 fused silica glass Substances 0.000 description 6
- 238000005259 measurement Methods 0.000 description 6
- 238000002156 mixing Methods 0.000 description 5
- 238000010306 acid treatment Methods 0.000 description 4
- 239000012298 atmosphere Substances 0.000 description 4
- 230000007547 defect Effects 0.000 description 4
- 238000009826 distribution Methods 0.000 description 4
- 150000003949 imides Chemical class 0.000 description 4
- 238000013001 point bending Methods 0.000 description 4
- 235000012239 silicon dioxide Nutrition 0.000 description 4
- 229910004298 SiO 2 Inorganic materials 0.000 description 3
- 229910052681 coesite Inorganic materials 0.000 description 3
- 229910052906 cristobalite Inorganic materials 0.000 description 3
- 238000005261 decarburization Methods 0.000 description 3
- 238000003795 desorption Methods 0.000 description 3
- 150000004767 nitrides Chemical class 0.000 description 3
- 229910052682 stishovite Inorganic materials 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 229910052905 tridymite Inorganic materials 0.000 description 3
- HLLSOEKIMZEGFV-UHFFFAOYSA-N 4-(dibutylsulfamoyl)benzoic acid Chemical compound CCCCN(CCCC)S(=O)(=O)C1=CC=C(C(O)=O)C=C1 HLLSOEKIMZEGFV-UHFFFAOYSA-N 0.000 description 2
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- 238000002441 X-ray diffraction Methods 0.000 description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 2
- 238000001354 calcination Methods 0.000 description 2
- 238000000354 decomposition reaction Methods 0.000 description 2
- 229910001873 dinitrogen Inorganic materials 0.000 description 2
- 238000011156 evaluation Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000001307 helium Substances 0.000 description 2
- 229910052734 helium Inorganic materials 0.000 description 2
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 2
- 238000010191 image analysis Methods 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 238000010298 pulverizing process Methods 0.000 description 2
- 239000007858 starting material Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 1
- 238000007088 Archimedes method Methods 0.000 description 1
- KZBUYRJDOAKODT-UHFFFAOYSA-N Chlorine Chemical compound ClCl KZBUYRJDOAKODT-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 229910003910 SiCl4 Inorganic materials 0.000 description 1
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- 239000006231 channel black Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 229910002026 crystalline silica Inorganic materials 0.000 description 1
- 238000000280 densification Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000006232 furnace black Substances 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 229910052736 halogen Inorganic materials 0.000 description 1
- 150000002367 halogens Chemical class 0.000 description 1
- 238000007731 hot pressing Methods 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 238000004255 ion exchange chromatography Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000004570 mortar (masonry) Substances 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- -1 polyethylene Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 150000004760 silicates Chemical class 0.000 description 1
- FDNAPBUWERUEDA-UHFFFAOYSA-N silicon tetrachloride Chemical compound Cl[Si](Cl)(Cl)Cl FDNAPBUWERUEDA-UHFFFAOYSA-N 0.000 description 1
- 239000011863 silicon-based powder Substances 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 230000002194 synthesizing effect Effects 0.000 description 1
- 238000003826 uniaxial pressing Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B21/00—Nitrogen; Compounds thereof
- C01B21/06—Binary 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
- C01B21/068—Binary 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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- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
- C04B35/515—Shaped 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
- C04B35/58—Shaped 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
- C04B35/584—Shaped 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
- C04B35/587—Fine ceramics
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Description
本開示は、窒化ケイ素粉末及びその製造方法、並びに、窒化ケイ素焼結体の製造方法に関する。 The present disclosure relates to silicon nitride powder and a method for producing the same, as well as 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。このため、ガスタービン、ターボロータ、及びバルブ等の機械部品、並びに、自動車及び工作機械等のパワーモジュール等の絶縁基板として窒化ケイ素焼結体を用いることが検討されている。これらの用途に用いられる窒化ケイ素焼結体には、緻密且つ均質な組織を有することが求められる。このような窒化ケイ素焼結体を製造するために、高純度且つ均質な窒化ケイ素粉末を提供する技術が検討されている。 Silicon nitride is a material with excellent strength, hardness, toughness, heat resistance, corrosion resistance, and thermal shock resistance. For this reason, the use of silicon nitride sintered bodies as insulating substrates for machine parts such as gas turbines, turbo rotors, and valves, as well as power modules for automobiles and machine tools, is being considered. Silicon nitride sintered bodies used for these applications are required to have a dense and homogeneous structure. In order to manufacture such silicon nitride sintered bodies, technologies to provide high-purity and homogeneous silicon nitride powder are being considered.
窒化ケイ素粉末の合成方法としては、金属ケイ素粉末を水素ガス又はアンモニアガスと窒素ガスとの混合雰囲気下で窒化する直接窒化法(直接反応法)、シリカ粉末の還元窒化法、及びイミド分解法等が知られている。特許文献1では、α型Si3N4の含有率が高い窒化ケイ素粉末を製造する方法が提案されている。また、特許文献2では、イミド分解法によって、不純物の少ない窒化ケイ素粉末を製造することが提案されている。 Known methods for synthesizing silicon nitride powder include a direct nitridation method (direct reaction method) in which metal silicon powder is nitrided in a mixed atmosphere of hydrogen gas or ammonia gas and nitrogen gas, a reduction nitridation method of silica powder, and an imide decomposition method. Patent Document 1 proposes a method for producing silicon nitride powder with a high content of α-type Si 3 N 4. Patent Document 2 proposes the production of silicon nitride powder with fewer impurities by the imide decomposition method.
窒化ケイ素焼結体は、高温環境下でも用いられる場合があるため、高温下での強度(高温強度)に優れることが求められる。高温強度向上のためには窒化ケイ素焼結体を緻密にする必要があると考えられる。窒化ケイ素焼結体の緻密化を妨げる因子としては、原料、すなわち窒化ケイ素粉末に含まれる不純物の影響が考えられる。 Silicon nitride sintered bodies are sometimes used in high-temperature environments, so they are required to have excellent strength at high temperatures (high-temperature strength). It is believed that in order to improve high-temperature strength, it is necessary to make the silicon nitride sintered body dense. One factor that may hinder the densification of silicon nitride sintered bodies is thought to be the influence of impurities contained in the raw material, i.e., silicon nitride powder.
そこで、本開示では、不純物を低減することによって、優れた高温強度を有する窒化ケイ素焼結体を製造することが可能な窒化ケイ素粉末を提供する。また、十分に不純物が低減された窒化ケイ素粉末を低い製造コストで製造することが可能な窒化ケイ素粉末の製造方法を提供する。また、優れた高温強度を有する窒化ケイ素焼結体を低い製造コストで製造することが可能な窒化ケイ素焼結体の製造方法を提供する。 In this disclosure, therefore, there is provided a silicon nitride powder capable of producing a silicon nitride sintered body having excellent high-temperature strength by reducing impurities. In addition, there is provided a method for producing silicon nitride powder capable of producing silicon nitride powder with sufficiently reduced impurities at low production cost. In addition, there is provided a method for producing silicon nitride sintered body capable of producing a silicon nitride sintered body having excellent high-temperature strength at low production cost.
本開示の一側面に係る窒化ケイ素粉末は、酸素含有量が3.0質量%以下、並びに、フッ素及び塩素の合計含有量が25質量ppm以下である。このような窒化ケイ素粉末は、高温強度に影響する酸素とフッ素及び塩素の含有量が十分に低いことから、高温強度に優れる窒化ケイ素焼結体を製造することができる。The silicon nitride powder according to one aspect of the present disclosure has an oxygen content of 3.0 mass% or less and a total fluorine and chlorine content of 25 mass ppm or less. Such silicon nitride powder has a sufficiently low content of oxygen, fluorine, and chlorine, which affect high-temperature strength, and therefore can produce a silicon nitride sintered body having excellent high-temperature strength.
上記窒化ケイ素粉末のα化率は92質量%以上であることが好ましい。高いα化率を有することによって、窒化ケイ素粉末の焼結時における粒成長を促進することができる。これによって、十分に緻密化された窒化ケイ素焼結体を製造することができる。したがって、一層優れた高温強度を有する窒化ケイ素焼結体を得ることができる。The alpha conversion rate of the silicon nitride powder is preferably 92% by mass or more. By having a high alpha conversion rate, grain growth during sintering of the silicon nitride powder can be promoted. This makes it possible to produce a sufficiently densified silicon nitride sintered body. Therefore, it is possible to obtain a silicon nitride sintered body having even better high-temperature strength.
上記窒化ケイ素粉末において、2μm以上の粒径を有する一次粒子の割合は2%以下であることが好ましい。これによって、窒化ケイ素粉末を焼結して得られる窒化ケイ素焼結体の微細組織を一層均一にすることができる。したがって、一層優れた高温強度を有する窒化ケイ素焼結体を得ることができる。In the above silicon nitride powder, it is preferable that the proportion of primary particles having a particle size of 2 μm or more is 2% or less. This makes it possible to make the microstructure of the silicon nitride sintered body obtained by sintering the silicon nitride powder more uniform. Therefore, it is possible to obtain a silicon nitride sintered body having even better high-temperature strength.
本開示の一側面に係る窒化ケイ素粉末の製造方法は、シリカ粉末とカーボン粉末と窒化ケイ素の種結晶とを含む原料粉末を、窒素雰囲気中、1300~1550℃で50時間以上焼成して窒化ケイ素粉末を得る焼成工程を有する。この製造方法では、焼成工程において、原料粉末を1300~1550℃で十分に長い時間焼成しているため、シリカ粉末の還元窒化反応が十分に進行する。したがって、十分に不純物が低減された窒化ケイ素粉末を製造することができる。この製造方法は、イミド法に比べて窒化ケイ素粉末の製造コストを低減することができる。また、直接窒化法では微粉化するために通常粉砕が必要となるが、粉砕に由来する不純物を低減するためには酸処理が必要となる。この場合、酸処理の薬液成分が残留して不純物となる。よって、本開示の窒化ケイ素粉末の製造方法によれば、十分に不純物が低減された窒化ケイ素粉末を低い製造コストで製造することができる。The method for producing silicon nitride powder according to one aspect of the present disclosure includes a calcination step in which raw powder containing silica powder, carbon powder, and silicon nitride seed crystals is calcined in a nitrogen atmosphere at 1300 to 1550 ° C for 50 hours or more to obtain silicon nitride powder. In this production method, the raw powder is calcined at 1300 to 1550 ° C for a sufficiently long time in the calcination step, so that the reduction-nitridation reaction of the silica powder proceeds sufficiently. Therefore, silicon nitride powder with sufficiently reduced impurities can be produced. This production method can reduce the production cost of silicon nitride powder compared to the imide method. In addition, in the direct nitridation method, crushing is usually required to finely pulverize, but acid treatment is required to reduce impurities derived from crushing. In this case, the chemical components of the acid treatment remain and become impurities. Therefore, according to the method for producing silicon nitride powder of the present disclosure, silicon nitride powder with sufficiently reduced impurities can be produced at low production costs.
上述の焼成工程で得られる窒化ケイ素粉末の酸素含有量は3.0質量%以下、並びに、フッ素及び塩素の合計含有量は25質量ppm以下であることが好ましい。このような窒化ケイ素粉末を用いることによって、優れた高温強度を有する窒化ケイ素焼結体を製造することができる。It is preferable that the oxygen content of the silicon nitride powder obtained by the above-mentioned firing process is 3.0 mass% or less, and the total content of fluorine and chlorine is 25 mass ppm or less. By using such silicon nitride powder, it is possible to produce a silicon nitride sintered body having excellent high-temperature strength.
上述の焼成工程で得られる窒化ケイ素粉末は、2μm以上の粒径を有する一次粒子の割合が2%以下であることが好ましい。これによって、窒化ケイ素粉末を焼成して得られる窒化ケイ素焼結体の微細組織を一層均一にすることができる。したがって、一層優れた高温強度を有する窒化ケイ素焼結体を得ることができる。本開示における上述の一次粒子の割合は、個数基準である。It is preferable that the silicon nitride powder obtained by the above-mentioned firing process has a proportion of primary particles having a particle size of 2 μm or more of 2% or less. This makes it possible to make the microstructure of the silicon nitride sintered body obtained by firing the silicon nitride powder more uniform. Therefore, it is possible to obtain a silicon nitride sintered body having even better high-temperature strength. The proportion of primary particles described above in this disclosure is based on the number of particles.
本開示の一側面に係る窒化ケイ素焼結体の製造方法は、上述のいずれかの窒化ケイ素粉末、又は上述のいずれかの製造方法で得られる窒化ケイ素粉末を焼成して窒化ケイ素焼結体を得る焼結工程を有する。この製造方法では、不純物が低減された窒化ケイ素粉末を焼結することから、優れた高温強度を有する窒化ケイ素焼結体を製造することができる。A method for producing a silicon nitride sintered body according to one aspect of the present disclosure includes a sintering step of sintering any of the silicon nitride powders described above, or silicon nitride powder obtained by any of the production methods described above, to obtain a silicon nitride sintered body. In this production method, silicon nitride powder with reduced impurities is sintered, so that a silicon nitride sintered body having excellent high-temperature strength can be produced.
本開示によれば、不純物を低減することによって、優れた高温強度を有する窒化ケイ素焼結体を製造することが可能な窒化ケイ素粉末を提供することができる。また、十分に不純物が低減された窒化ケイ素粉末を低い製造コストで製造することが可能な窒化ケイ素粉末の製造方法を提供することができる。また、優れた高温強度を有する窒化ケイ素焼結体を低い製造コストで製造することが可能な窒化ケイ素焼結体の製造方法を提供することができる。 According to the present disclosure, it is possible to provide silicon nitride powder capable of producing silicon nitride sintered bodies having excellent high-temperature strength by reducing impurities. It is also possible to provide a method for producing silicon nitride powder capable of producing silicon nitride powder with sufficiently reduced impurities at low production costs. It is also possible to provide a method for producing silicon nitride sintered bodies capable of producing silicon nitride sintered bodies having excellent high-temperature strength at low production costs.
以下、本開示の一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。An embodiment of the present disclosure will be described below. However, the following embodiment is an example for explaining the present disclosure, and is not intended to limit the present disclosure to the following content.
一実施形態に係る窒化ケイ素粉末は、酸素含有量が3.0質量%以下、並びに、フッ素及び塩素の合計含有量が25質量ppm以下である。酸素含有量は、一層優れた高温強度を有する窒化ケイ素焼結体を製造可能とする観点から、2.5質量%以下であってよく、2.3質量%以下であってよく、1.8質量%以下でああってもよい。窒化ケイ素粉末の酸素含有量を低減することによって、窒化ケイ素粉末を焼結して得られる窒化ケイ素焼結体の内部の欠陥を低減することができる。これによって、十分に高い高温強度を有する窒化ケイ素焼結体を得ることができる。酸素含有量は、窒化ケイ素粉末を製造する際の焼成時間、及び、窒化ケイ素粉末を製造する際に用いる出発原料におけるカーボン粉末の配合割合に依存する傾向にある。The silicon nitride powder according to one embodiment has an oxygen content of 3.0% by mass or less, and a total content of fluorine and chlorine of 25 ppm by mass or less. The oxygen content may be 2.5% by mass or less, 2.3% by mass or less, or 1.8% by mass or less, from the viewpoint of being able to produce a silicon nitride sintered body having even better high-temperature strength. By reducing the oxygen content of the silicon nitride powder, it is possible to reduce internal defects in the silicon nitride sintered body obtained by sintering the silicon nitride powder. This makes it possible to obtain a silicon nitride sintered body having sufficiently high high-temperature strength. The oxygen content tends to depend on the firing time when producing the silicon nitride powder and the blending ratio of carbon powder in the starting material used when producing the silicon nitride powder.
窒化ケイ素粉末の酸素含有量は、窒化ケイ素粉末の製造コスト低減の観点から、0.1質量%以上であってよいし、0.5質量%以上であってもよい。窒化ケイ素粉末の酸素含有量の一例は、0.1~3.0質量%であってよく、0.5~2.5質量%であってもよい。窒化ケイ素粉末の酸素含有量は、市販の酸素・窒素分析装置を用いて測定することができる。測定は、ヘリウムガスの雰囲気中、20℃から3000℃まで連続的に昇温して行う。得られた測定結果のうち、酸素の脱離に由来するピークの面積から酸素含有量を定量することができる。From the viewpoint of reducing the manufacturing cost of silicon nitride powder, the oxygen content of the silicon nitride powder may be 0.1% by mass or more, or may be 0.5% by mass or more. An example of the oxygen content of the silicon nitride powder may be 0.1 to 3.0% by mass, or may be 0.5 to 2.5% by mass. The oxygen content of the silicon nitride powder can be measured using a commercially available oxygen/nitrogen analyzer. The measurement is performed in an atmosphere of helium gas, by continuously raising the temperature from 20°C to 3000°C. The oxygen content can be quantified from the area of the peak resulting from the desorption of oxygen from the obtained measurement results.
窒化ケイ素粉末のフッ素及び塩素の合計含有量は、一層優れた高温強度を有する窒化ケイ素焼結体を製造可能とする観点から、22質量ppm以下であってよく、20質量ppm以下であってよく、19質量ppm以下であってよい。窒化ケイ素粉末のフッ素及び塩素の合計含有量を低減することによって、窒化ケイ素粉末を焼結して得られる窒化ケイ素焼結体の粒界相に含まれるフッ素及び塩素が低減される。このため、高温下で窒化ケイ素焼結体の粒界相が軟化すること抑制できる。したがって、十分に高い高温強度を有する窒化ケイ素焼結体とすることができる。フッ素及び塩素の合計含有量は、窒化ケイ素粉末を製造する際に用いる出発原料の純度、シリカ粉末とカーボン粉末の配合比(C/SiO2)、焼成時間、及び焼成後の後処理(洗浄)の有無等に依存する傾向にある。 The total content of fluorine and chlorine in the silicon nitride powder may be 22 mass ppm or less, 20 mass ppm or less, or 19 mass ppm or less, from the viewpoint of being able to produce a silicon nitride sintered body having even better high-temperature strength. By reducing the total content of fluorine and chlorine in the silicon nitride powder, the fluorine and chlorine contained in the grain boundary phase of the silicon nitride sintered body obtained by sintering the silicon nitride powder is reduced. Therefore, the grain boundary phase of the silicon nitride sintered body can be suppressed from softening at high temperatures. Therefore, it is possible to obtain a silicon nitride sintered body having sufficiently high high-temperature strength. The total content of fluorine and chlorine tends to depend on the purity of the starting material used in producing the silicon nitride powder, the compounding ratio of the silica powder and the carbon powder (C/SiO 2 ), the firing time, and the presence or absence of post-treatment (washing) after firing.
例えば、原料粉末を調製する際のシリカ粉末とカーボン粉末の配合比(C/SiO2)が小さくなり過ぎると、SiO2又はSiOとCl2との反応によるSiCl4の脱離が進行し難くなる傾向にある。また、焼成時間が短くなり過ぎた場合も同様の傾向にある。 For example, if the compounding ratio of silica powder to carbon powder (C/ SiO2 ) when preparing the raw material powder is too small, the desorption of SiCl4 due to the reaction of SiO2 or SiO with Cl2 tends to be difficult to proceed. The same tendency also occurs when the firing time is too short.
窒化ケイ素粉末のフッ素及び塩素の合計含有量は、窒化ケイ素粉末の製造コスト低減の観点から、1質量ppm以上であってよいし、5質量ppm以上であってもよい。窒化ケイ素粉末のフッ素及び塩素の合計含有量の一例は、1~25質量ppmであってよく、5~22質量ppmであってもよい。窒化ケイ素粉末のフッ素及び塩素の合計含有量は、窒化ケイ素粉末を加熱し、発生したガスに含まれるフッ素及び塩素をイオンクロマトグラフで定量することによって測定することができる。From the viewpoint of reducing the manufacturing cost of silicon nitride powder, the total fluorine and chlorine content of the silicon nitride powder may be 1 ppm by mass or more, or may be 5 ppm by mass or more. An example of the total fluorine and chlorine content of the silicon nitride powder may be 1 to 25 ppm by mass, or may be 5 to 22 ppm by mass. The total fluorine and chlorine content of the silicon nitride powder can be measured by heating the silicon nitride powder and quantifying the fluorine and chlorine contained in the generated gas by ion chromatography.
窒化ケイ素粉末のα化率は、92質量%以上であってよく、95質量%以上であってよく、96質量%以上であってもよい。高いα化率を有することによって、窒化ケイ素粉末の焼結時に粒成長を促進することができる。これによって、十分に緻密化された窒化ケイ素焼結体を製造することができる。したがって、一層優れた高温強度を有する窒化ケイ素焼結体を得ることができる。The alpha-conversion rate of the silicon nitride powder may be 92% by mass or more, 95% by mass or more, or 96% by mass or more. By having a high alpha-conversion rate, grain growth can be promoted during sintering of the silicon nitride powder. This makes it possible to produce a sufficiently densified silicon nitride sintered body. Therefore, it is possible to obtain a silicon nitride sintered body having even better high-temperature strength.
窒化ケイ素粉末のα化率は、窒化ケイ素粉末の製造コスト低減の観点から、99質量%以下であってよいし、98質量%以下であってもよい。窒化ケイ素粉末のα化率の一例は、92~99質量%であってよく、95~99質量%であってよく、96~98質量%であってもよい。窒化ケイ素粉末のα化率は、X線回折の回折線強度に基づいて求めることができる。From the viewpoint of reducing the manufacturing cost of silicon nitride powder, the alpha conversion rate of the silicon nitride powder may be 99% by mass or less, or may be 98% by mass or less. An example of the alpha conversion rate of the silicon nitride powder may be 92 to 99% by mass, 95 to 99% by mass, or 96 to 98% by mass. The alpha conversion rate of the silicon nitride powder can be determined based on the diffraction line intensity of X-ray diffraction.
窒化ケイ素粉末に含まれる一次粒子のうち、2μm以上の粒径を有する一次粒子の割合は好ましくは2%以下である。当該割合は、1%以下であってよいし、0.5%以下であってもよい。この割合を小さくすることによって、窒化ケイ素粉末を焼結して得られる窒化ケイ素焼結体の微細組織を一層均一にすることができる。したがって、一層優れた高温強度を有する窒化ケイ素焼結体を得ることができる。Of the primary particles contained in the silicon nitride powder, the proportion of primary particles having a particle size of 2 μm or more is preferably 2% or less. This proportion may be 1% or less, or may be 0.5% or less. By reducing this proportion, the microstructure of the silicon nitride sintered body obtained by sintering the silicon nitride powder can be made more uniform. Therefore, it is possible to obtain a silicon nitride sintered body with even superior high-temperature strength.
窒化ケイ素粉末に含まれる一次粒子のうち、2μm以上の粒径を有する一次粒子の割合は、窒化ケイ素粉末の製造コスト低減の観点から、0.1%以上であってよいし、0.3%以上であってもよい。上記割合の一例は、0.1~2%であってよく、0.3~1%であってもよい。上記割合は、個数基準の割合であり、走査型電子顕微鏡の撮影画像を、画像解析式粒度分布測定ソフトウェアに取り込んで測定される粒度分布に基づいて求めることができる。From the viewpoint of reducing the manufacturing cost of silicon nitride powder, the proportion of primary particles having a particle size of 2 μm or more among the primary particles contained in the silicon nitride powder may be 0.1% or more, or may be 0.3% or more. One example of the above proportion may be 0.1 to 2%, or 0.3 to 1%. The above proportion is a proportion based on the number, and can be determined based on the particle size distribution measured by importing an image taken with a scanning electron microscope into image analysis particle size distribution measurement software.
窒化ケイ素粉末は、窒化ケイ素以外の成分として、炭素又は炭化物を含んでいてもよい。窒化ケイ素粉末における炭素及び炭化物の合計含有量は、炭素換算で、好ましくは10質量%以下であり、より好ましくは7質量%以下である。The silicon nitride powder may contain carbon or carbide as a component other than silicon nitride. The total content of carbon and carbide in the silicon nitride powder is preferably 10 mass% or less, more preferably 7 mass% or less, calculated as carbon.
一実施形態に係る窒化ケイ素粉末の製造方法は、シリカ粉末とカーボン粉末と窒化ケイ素の種結晶とを配合して原料粉末を調製する配合工程と、原料粉末を窒素雰囲気中、1300~1550℃で50時間以上焼成して窒化ケイ素粉末を得る焼成工程を有する。焼成時間は、生産効率の観点から例えば200時間以下であってよい。シリカ粉末としては、例えば、溶融シリカ粉末、結晶性のシリカ粉末及びケイ酸塩化合物が挙げられる。カーボン粉末としては、アセチレンブラック、ファーネスブラック、チャンネルブラック、及び黒鉛が挙げられる。種結晶として用いる窒化ケイ素は、焼結性を高くする観点から、α化率が高い(例えば、α化率が90%以上)ものが好ましい。 The method for producing silicon nitride powder according to one embodiment includes a blending step of blending silica powder, carbon powder, and silicon nitride seed crystals to prepare a raw material powder, and a firing step of firing the raw material powder in a nitrogen atmosphere at 1300 to 1550°C for 50 hours or more to obtain silicon nitride powder. The firing time may be, for example, 200 hours or less from the viewpoint of production efficiency. Examples of silica powder include fused silica powder, crystalline silica powder, and silicate compounds. Examples of carbon powder include acetylene black, furnace black, channel black, and graphite. The silicon nitride used as the seed crystals preferably has a high alpha conversion rate (for example, an alpha conversion rate of 90% or more) from the viewpoint of increasing sinterability.
配合工程における、シリカ粉末に対するカーボン粉末の配合比は、フッ素及び塩素の合計含有量と酸素含有量が十分に低減された窒化ケイ素粉末を得る観点から、モル基準(C/SiO2)で2.0~3.8であってよく、3.0~3.7であってもよい。シリカ粉末100質量部に対する窒化ケイ素の種結晶の配合量は、製造コストを低減しつつ純度が十分に高い窒化ケイ素粉末を得る観点から、10~20質量部であってよく、11~18質量部であってもよい。 The compounding ratio of the carbon powder to the silica powder in the compounding step may be 2.0 to 3.8, or may be 3.0 to 3.7, on a molar basis (C/SiO 2 ), from the viewpoint of obtaining silicon nitride powder in which the total content of fluorine and chlorine and the oxygen content are sufficiently reduced. The compounding amount of the silicon nitride seed crystals per 100 parts by mass of the silica powder may be 10 to 20 parts by mass, or may be 11 to 18 parts by mass, from the viewpoint of obtaining silicon nitride powder with sufficiently high purity while reducing production costs.
原料粉末中のフッ素及び塩素の合計含有量は、製造される窒化ケイ素粉末のフッ素及び塩素の合計含有量を十分に低減する観点から、好ましくは50質量ppm以下であり、より好ましくは40質量ppm以下である。一方、原料粉末中のフッ素及び塩素の合計含有量は、窒化ケイ素粉末の製造コストを低減する観点から、10質量ppm以上であってよく、20質量ppm以上であってもよい。The total content of fluorine and chlorine in the raw material powder is preferably 50 ppm by mass or less, more preferably 40 ppm by mass or less, from the viewpoint of sufficiently reducing the total content of fluorine and chlorine in the silicon nitride powder to be produced. On the other hand, the total content of fluorine and chlorine in the raw material powder may be 10 ppm by mass or more, or may be 20 ppm by mass or more, from the viewpoint of reducing the production cost of the silicon nitride powder.
焼成工程では、例えば電気炉を用いて原料粉末を焼成することによって、以下の反応式(1)が進行する。反応式(1)の反応を十分に進行させる観点から、焼成温度は1450~1550℃であってもよい。焼成時間は、シリカ粉末の還元窒化反応を十分に進行させる観点から、150時間以上であってよく、200時間以上であってもよい。一方、焼成時間は、窒化ケイ素粉末の製造コストを低減する観点から、500時間以下であってよく、400時間以下であってもよい。
3SiO2+6C+2N2→Si3N4+6CO↑ (1)
In the firing step, the raw material powder is fired using, for example, an electric furnace, whereby the following reaction formula (1) proceeds. From the viewpoint of sufficiently proceeding with the reaction of reaction formula (1), the firing temperature may be 1450 to 1550° C. From the viewpoint of sufficiently proceeding with the reduction-nitridation reaction of the silica powder, the firing time may be 150 hours or more, or may be 200 hours or more. On the other hand, from the viewpoint of reducing the production cost of the silicon nitride powder, the firing time may be 500 hours or less, or may be 400 hours or less.
3SiO 2 +6C+2N 2 →Si 3 N 4 +6CO↑ (1)
焼成工程は、窒素雰囲気中で行う。窒素雰囲気における酸素濃度は、100体積ppm以下であってよく、20体積ppm以下であってもよい。窒素雰囲気における酸素濃度を十分に低くすることによって、製造される窒化ケイ素粉末の酸素含有量を一層低減することができる。窒化ケイ素粉末が炭素又は炭化物を含む場合、脱炭工程を行ってもよい。脱炭工程は、例えば、窒化ケイ素粉末を大気中において650~900℃に加熱して行うことができる。これによって、窒化ケイ素粉末における炭素及び炭化物の合計含有量を低くすることができる。The firing process is carried out in a nitrogen atmosphere. The oxygen concentration in the nitrogen atmosphere may be 100 ppm by volume or less, or may be 20 ppm by volume or less. By sufficiently lowering the oxygen concentration in the nitrogen atmosphere, the oxygen content of the silicon nitride powder produced can be further reduced. If the silicon nitride powder contains carbon or carbide, a decarburization process may be carried out. The decarburization process can be carried out, for example, by heating the silicon nitride powder to 650 to 900°C in air. This allows the total carbon and carbide content in the silicon nitride powder to be reduced.
上述の製造方法によれば、上記実施形態に係る窒化ケイ素粉末を得ることができる。窒化ケイ素粉末の酸素含有量、フッ素及び塩素の合計含有量、α化率及び粒径等の性状の例は、上述したとおりである。本実施形態の窒化ケイ素粉末の製造方法では、シリカ粉末の還元窒化反応によって窒化ケイ素粉末を製造する。したがって、イミド法に比べて窒化ケイ素粉末の製造コストを低減することができる。また、直接窒化法では微粉化するために通常粉砕が必要となるが、粉砕に由来する不純物を低減するためには酸処理が必要となる。この場合、酸処理の薬液成分が残留して不純物となる。よって、本開示の窒化ケイ素粉末の製造方法によれば、十分に不純物が低減された窒化ケイ素粉末を低い製造コストで製造することができる。According to the above-mentioned manufacturing method, the silicon nitride powder according to the above-mentioned embodiment can be obtained. Examples of properties such as the oxygen content, the total content of fluorine and chlorine, the alpha conversion rate, and the particle size of the silicon nitride powder are as described above. In the manufacturing method of silicon nitride powder of this embodiment, silicon nitride powder is manufactured by a reduction-nitridation reaction of silica powder. Therefore, the manufacturing cost of silicon nitride powder can be reduced compared to the imide method. In addition, in the direct nitridation method, pulverization is usually required to pulverize the powder, but acid treatment is required to reduce impurities derived from pulverization. In this case, the chemical components of the acid treatment remain and become impurities. Therefore, according to the manufacturing method of silicon nitride powder disclosed herein, silicon nitride powder with sufficiently reduced impurities can be manufactured at a low manufacturing cost.
一実施形態に係る窒化ケイ素焼結体の製造方法は、上記実施形態に係る窒化ケイ素粉末を焼成して窒化ケイ素焼結体を得る焼結工程を有する。この製造方法では、例えば、窒化ケイ素粉末を例えば3.0~10.0MPa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。 The method for producing a silicon nitride sintered body according to one embodiment includes a sintering step in which the silicon nitride powder according to the above embodiment is sintered to obtain a silicon nitride sintered body. In this production method, for example, the silicon nitride powder is pressed at a molding pressure of, for example, 3.0 to 10.0 MPa to obtain a molded body. The molded body may be produced by uniaxial pressing or by CIP. It may also be sintered while being molded by hot pressing.
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、0.7~0.9MPaであってよい。焼成温度は1700~1900℃であってよい。当該焼成温度における焼成時間は4~20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。 The sintering of the molded body may be carried out in an inert gas atmosphere such as nitrogen gas or argon gas. The pressure during sintering may be 0.7 to 0.9 MPa. The sintering temperature may be 1700 to 1900°C. The sintering time at the sintering temperature may be 4 to 20 hours, or 8 to 16 hours. The rate of temperature rise to the sintering temperature may be, for example, 1.0 to 10.0°C/hour.
このようにして得られる窒化ケイ素焼結体は、酸素含有量及びフッ素及び塩素の合計含有量が十分に低減されている。酸素含有量が十分に低減されているため、窒化ケイ素焼結体の内部に生じる欠陥を抑制できる。このため、高温強度のみならず絶縁性及び熱伝導性にも優れる。窒化ケイ素焼結体に含まれる欠陥としては、転位等の格子欠陥及び気孔等が考えられる。また、フッ素及び塩素の合計含有量が十分に低減されているため、高温下で窒化ケイ素焼結体の粒界相が軟化することを抑制できる。したがって、十分に高い高温強度を有する窒化ケイ素焼結体を得ることができる。The silicon nitride sintered body obtained in this manner has a sufficiently reduced oxygen content and a sufficiently reduced total content of fluorine and chlorine. Because the oxygen content is sufficiently reduced, defects occurring inside the silicon nitride sintered body can be suppressed. This results in excellent high-temperature strength as well as insulation and thermal conductivity. Defects contained in the silicon nitride sintered body include lattice defects such as dislocations and pores. In addition, because the total content of fluorine and chlorine is sufficiently reduced, softening of the grain boundary phase of the silicon nitride sintered body at high temperatures can be suppressed. Therefore, a silicon nitride sintered body having sufficiently high high-temperature strength can be obtained.
本開示における高温強度とは、1300℃における強度をいう。このような温度範囲において高い強度を有する窒化ケイ素焼結体は、ガスタービン、自動車用のパワーモジュール、ベアリング等の用途に特に好適に用いることができる。一実施形態に係る窒化ケイ素焼結体の1300℃の温度における曲げ強度は、例えば700MPa以上であってよく、750MPa以上であってもよい。この強度は、市販の測定装置を用いて測定される4点曲げ強度(1300℃)である。In this disclosure, high-temperature strength refers to strength at 1300°C. Silicon nitride sintered bodies having high strength in such a temperature range can be particularly suitably used in applications such as gas turbines, automotive power modules, and bearings. The bending strength of the silicon nitride sintered body according to one embodiment at a temperature of 1300°C may be, for example, 700 MPa or more, or 750 MPa or more. This strength is the four-point bending strength (1300°C) measured using a commercially available measuring device.
以上、幾つかの実施形態を説明したが、本開示は上述の実施形態に何ら限定されるものではない。例えば、窒化ケイ素粉末は、窒化ケイ素焼結体の製造用以外の用途に用いてもよい。Although several embodiments have been described above, the present disclosure is not limited to the above-described embodiments. For example, the silicon nitride powder may be used for purposes other than the manufacture of silicon nitride sintered bodies.
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が、本開示は下記の実施例に限定されるものではない。The contents of the present disclosure will be explained in more detail with reference to examples and comparative examples, but the present disclosure is not limited to the examples below.
<窒化ケイ素粉末の調製>
(実施例1)
溶融シリカ粉末(粒径:0.6μm)、アセチレンブラック粉末、及び、窒化ケイ素粉末(種結晶)を配合して原料粉末を得た。原料粉末中のフッ素及び塩素の合計含有量は、40質量ppmであった。配合比(質量基準)は、溶融シリカ粉末:アセチレンブラック粉末:窒化ケイ素粉末=55.2%:38.5%:6.3%とした。溶融シリカ粉末に対するアセチレンブラックのモル比(C/SiO2)は3.5であった。この原料粉末320gを、2Lのポリエチレン製容器に充填して窒化ケイ素製ボール(φ:15mm)を入れ、ボールミルで2時間混合した。
<Preparation of silicon nitride powder>
Example 1
A raw material powder was obtained by blending fused silica powder (particle size: 0.6 μm), acetylene black powder, and silicon nitride powder (seed crystals). The total content of fluorine and chlorine in the raw material powder was 40 ppm by mass. The blending ratio (mass basis) was fused silica powder: acetylene black powder: silicon nitride powder = 55.2%: 38.5%: 6.3%. The molar ratio (C/SiO 2 ) of acetylene black to fused silica powder was 3.5. 320 g of this raw material powder was filled into a 2 L polyethylene container, silicon nitride balls (φ: 15 mm) were added, and the mixture was mixed in a ball mill for 2 hours.
原料粉末を、電気炉を用いて大気圧の窒素雰囲気中、1500℃で60時間焼成し、塊状の窒化物を得た。この窒化物を窒化ケイ素製の乳鉢で解砕して窒化物粉末を得た。これをアルミナ坩堝に入れ、電気炉中、800℃で3時間加熱して脱炭した。脱炭して得られた脱炭粉を窒化ケイ素製のボールとともにアルミナポットに充填し、振動ミルで3時間粉砕して、窒化ケイ素粉末を得た。The raw material powder was fired in an electric furnace in a nitrogen atmosphere at atmospheric pressure at 1500°C for 60 hours to obtain lump nitride. This nitride was crushed in a silicon nitride mortar to obtain nitride powder. This was placed in an alumina crucible and heated in an electric furnace at 800°C for 3 hours to decarburize. The decarburized powder obtained by decarburization was loaded into an alumina pot together with silicon nitride balls and pulverized in a vibrating mill for 3 hours to obtain silicon nitride powder.
(実施例2)
原料粉末を1500℃で焼成する時間を、60時間から110時間に変更したこと以外は、実施例1と同様にして窒化ケイ素粉末を得た。
Example 2
Silicon nitride powder was obtained in the same manner as in Example 1, except that the time for sintering the raw material powder at 1500° C. was changed from 60 hours to 110 hours.
(比較例1)
原料粉末を1500℃で焼成する時間を、60時間から10時間に変更したこと以外は、実施例1と同様にして窒化ケイ素粉末を得た。
(Comparative Example 1)
Silicon nitride powder was obtained in the same manner as in Example 1, except that the time for sintering the raw material powder at 1500° C. was changed from 60 hours to 10 hours.
(比較例2)
配合比(質量基準)を、溶融シリカ粉末:アセチレンブラック粉末:窒化ケイ素粉末=52.3%:41.7%:6.0%としたこと以外は、実施例2と同様にして窒化ケイ素粉末を得た。溶融シリカ粉末に対するアセチレンブラックのモル比(C/SiO2)は4.0であった。
(Comparative Example 2)
A silicon nitride powder was obtained in the same manner as in Example 2, except that the compounding ratio (by mass) of fused silica powder: acetylene black powder: silicon nitride powder was 52.3%: 41.7%: 6.0%. The molar ratio of acetylene black to fused silica powder (C/ SiO2 ) was 4.0.
(比較例3)
原料粉末を1500℃で焼成する時間を、60時間から5時間に変更したこと以外は、実施例1と同様にして窒化ケイ素粉末を得た。
(Comparative Example 3)
Silicon nitride powder was obtained in the same manner as in Example 1, except that the time for sintering the raw material powder at 1500° C. was changed from 60 hours to 5 hours.
<窒化ケイ素粉末の評価>
各実施例及び比較例の窒化ケイ素粉末に含まれる酸素含有量を以下の手順で測定した。酸素・窒素分析装置(堀場製作所製、装置名:EMGA-920W)を用いて、黒鉛粉末を入れた坩堝の脱ガスを行った。調製した窒化ケイ素粉末を秤量し、坩堝中の黒鉛粉末と混合した。その後、ヘリウムガスの雰囲気中、20℃から2300℃まで昇温し、昇温に伴って生じる酸素を検知した。酸素の脱離に由来するピーク面積から、窒化ケイ素粉末に含まれる酸素を定量した。測定結果は表1に示すとおりであった。
<Evaluation of Silicon Nitride Powder>
The oxygen content in the silicon nitride powder of each Example and Comparative Example was measured by the following procedure. The crucible containing the graphite powder was degassed using an oxygen/nitrogen analyzer (manufactured by Horiba, Ltd., device name: EMGA-920W). The prepared silicon nitride powder was weighed and mixed with the graphite powder in the crucible. Thereafter, the temperature was raised from 20°C to 2300°C in a helium gas atmosphere, and the oxygen generated with the temperature rise was detected. The amount of oxygen contained in the silicon nitride powder was quantified from the peak area resulting from the desorption of oxygen. The measurement results are shown in Table 1.
窒化ケイ素粉末に含まれるフッ素及び塩素の合計含有量を以下の手順で測定した。自動試料燃焼装置(三菱化学株式会社製、装置名:AQF-2100H型)を用いて窒化ケイ素粉末を加熱し、発生したガスを水に溶解させた。イオンクロマトグラフ(サーモフィッシャーサイエンティフィック社製、装置名:ICS-2100)を用いて、JIS R 1603:2007に準じて水中に溶解したフッ素及び塩素を測定した。この測定値に基づいて、窒化ケイ素粉末に含まれるフッ素及び塩素を定量した。測定結果は表1に示すとおりであった。表1中、「ハロゲン含有量」とは、フッ素と塩素の合計含有量である。The total fluorine and chlorine content in the silicon nitride powder was measured by the following procedure. The silicon nitride powder was heated using an automatic sample combustion device (Mitsubishi Chemical Corporation, device name: AQF-2100H type) and the generated gas was dissolved in water. The fluorine and chlorine dissolved in water were measured using an ion chromatograph (Thermo Fisher Scientific, device name: ICS-2100) in accordance with JIS R 1603:2007. Based on this measured value, the fluorine and chlorine contained in the silicon nitride powder were quantified. The measurement results are shown in Table 1. In Table 1, "halogen content" refers to the total content of fluorine and chlorine.
調製した窒化ケイ素粉末のα化率を以下の手順で測定した。X線回折装置(リガク製、装置名:Ultima IV)を用い、CuKα線で窒化ケイ素粉末のX線回折を行った。α相は(102)面の回折線強度Ia102と、(210)面の回折線強度Ia210、β相は(101)面の回折線強度Ib101と、(210)面の回折線強度Ib210で代表した。これらの回折線強度を用いて、以下の式によってα化率を算出した。結果は表1に示すとおりであった。
α化率(質量%)=
(Ia102+Ia210)/(Ia102+Ia210+Ib101+Ib210)×100
The alpha-phase ratio of the prepared silicon nitride powder was measured by the following procedure. X-ray diffraction of the silicon nitride powder was performed with CuKα radiation using an X-ray diffractometer (manufactured by Rigaku, device name: Ultima IV). The alpha phase was represented by the diffraction line intensity I a102 of the (102) plane and the diffraction line intensity I a210 of the (210) plane, and the beta phase was represented by the diffraction line intensity I b101 of the (101) plane and the diffraction line intensity I b210 of the (210) plane. Using these diffraction line intensities, the alpha-phase ratio was calculated by the following formula. The results were as shown in Table 1.
Alpha conversion rate (mass%) =
(I a102 +I a210 )/(I a102 +I a210 +I b101 +I b210 )×100
調製した窒化ケイ素粉末に含まれる、粒径2μm以上の粒子の割合を以下の手順で測定した。走査型電子顕微鏡(日本電子株式会社製、装置名:JSM-6301F)を用いて、窒化ケイ素粉末を5000倍に拡大して観察し、画像を撮影した(視野:16μm×23μm)。画像解析式粒度分布測定ソフトウェア(株式会社マウンテック製、製品名:Mac View version4.0)に撮影した画像を取り込み、粒度分布を測定した。測定結果から、粒径が2μm以上である一次粒子の割合を算出した。結果は表1に示すとおりであった。The proportion of particles with a particle size of 2 μm or more contained in the prepared silicon nitride powder was measured using the following procedure. Using a scanning electron microscope (manufactured by JEOL Ltd., device name: JSM-6301F), the silicon nitride powder was observed at 5000 times magnification and images were taken (field of view: 16 μm x 23 μm). The images taken were imported into image analysis type particle size distribution measurement software (manufactured by Mountec Co., Ltd., product name: Mac View version 4.0) and the particle size distribution was measured. From the measurement results, the proportion of primary particles with a particle size of 2 μm or more was calculated. The results are shown in Table 1.
<窒化ケイ素焼結体の作製>
各実施例及び比較例の窒化ケイ素粉末を、それぞれ一軸加圧成形し、円柱形状の成形体を作製した。この成形体を、カーボンヒータを備える電気炉中に配置し、窒素雰囲気中、1850℃まで昇温した。1850℃の焼成温度で6時間焼成を行った後、冷却して窒化ケイ素焼結体を得た。
<Preparation of sintered silicon nitride>
The silicon nitride powders of each Example and Comparative Example were each uniaxially pressed to produce a cylindrical molded body. The molded body was placed in an electric furnace equipped with a carbon heater and heated to 1850° C. in a nitrogen atmosphere. After sintering at 1850° C. for 6 hours, the body was cooled to obtain a silicon nitride sintered body.
<窒化ケイ素焼結体の評価>
得られた窒化ケイ素焼結体の密度(20℃)、及び1300℃における4点曲げ強度を測定した。密度は、アルキメデス法によって測定した。1300℃における4点曲げ強度は、株式会社島津製作所製のオートグラフAG-2000(商品名)を用いて測定した。実施例1の窒化ケイ素粉末を用いて作製した窒化ケイ素焼結体の測定結果を基準としたときの密度及び4点曲げ強度の相対値は、表1に示すとおりであった。
<Evaluation of sintered silicon nitride>
The density (20°C) and four-point bending strength at 1300°C of the obtained silicon nitride sintered body were measured. The density was measured by the Archimedes method. The four-point bending strength at 1300°C was measured using an Autograph AG-2000 (product name) manufactured by Shimadzu Corporation. The relative values of the density and four-point bending strength when the measurement results of the silicon nitride sintered body produced using the silicon nitride powder of Example 1 were used as the standard were as shown in Table 1.
酸素含有量が実施例1,2よりも高い比較例1,3は、高温強度が実施例1,2に比べて低かった。フッ素及び塩素の合計含有量が実施例1,2よりも高い比較例2も、高温強度が実施例1,2に比べて低かった。表1に示すとおり、酸素の含有量、並びにフッ素及び塩素の合計含有量が低い窒化ケイ素粉末を用いることによって、高温強度に優れた窒化ケイ素焼結体が得られることが確認された。 Comparative Examples 1 and 3, which had a higher oxygen content than Examples 1 and 2, had lower high-temperature strength than Examples 1 and 2. Comparative Example 2, which had a higher total fluorine and chlorine content than Examples 1 and 2, also had lower high-temperature strength than Examples 1 and 2. As shown in Table 1, it was confirmed that by using silicon nitride powder with a low oxygen content and a low total fluorine and chlorine content, a silicon nitride sintered body with excellent high-temperature strength can be obtained.
本開示によれば、不純物を低減することによって、高温強度に優れる窒化ケイ素焼結体を製造することが可能な窒化ケイ素粉末を提供することができる。また、十分に不純物が低減された窒化ケイ素粉末を低い製造コストで製造することが可能な窒化ケイ素粉末の製造方法を提供することができる。また、優れた高温強度を有する窒化ケイ素焼結体を低い製造コストで製造することが可能な窒化ケイ素焼結体の製造方法を提供することができる。 According to the present disclosure, it is possible to provide silicon nitride powder capable of producing silicon nitride sintered bodies having excellent high-temperature strength by reducing impurities. It is also possible to provide a method for producing silicon nitride powder capable of producing silicon nitride powder with sufficiently reduced impurities at low production costs. It is also possible to provide a method for producing silicon nitride sintered bodies capable of producing silicon nitride sintered bodies having excellent high-temperature strength at low production costs.
Claims (8)
炭素又は炭化物を含み、炭素及び炭化物の合計含有量が7質量%以下である、窒化ケイ素粉末。 The oxygen content is 1.2 to 3.0 mass%, the total content of fluorine and chlorine is 22 mass ppm or less, and the proportion of primary particles having a particle size of 2 μm or more is 2% or less,
A silicon nitride powder containing carbon or carbide, the total content of carbon and carbide being 7 mass% or less .
前記焼成工程で得られる前記窒化ケイ素粉末の酸素含有量は3.0質量%以下、並びに、フッ素及び塩素の合計含有量は25質量ppm以下である、窒化ケイ素粉末の製造方法。 A firing step of firing a raw material powder containing silica powder, carbon powder, and silicon nitride seed crystals in a nitrogen atmosphere at 1300 to 1550° C. for 50 hours or more to obtain silicon nitride powder,
A method for producing silicon nitride powder, wherein the silicon nitride powder obtained in the firing step has an oxygen content of 3.0 mass% or less, and a total fluorine and chlorine content of 25 mass ppm or less.
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