JPH07102966B2 - Method for manufacturing silicon nitride - Google Patents
Method for manufacturing silicon nitrideInfo
- Publication number
- JPH07102966B2 JPH07102966B2 JP1043079A JP4307989A JPH07102966B2 JP H07102966 B2 JPH07102966 B2 JP H07102966B2 JP 1043079 A JP1043079 A JP 1043079A JP 4307989 A JP4307989 A JP 4307989A JP H07102966 B2 JPH07102966 B2 JP H07102966B2
- Authority
- JP
- Japan
- Prior art keywords
- silicon nitride
- powder
- oxygen
- silicon
- nitriding
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 229910052581 Si3N4 Inorganic materials 0.000 title claims description 87
- HQVNEWCFYHHQES-UHFFFAOYSA-N silicon nitride Chemical compound N12[Si]34N5[Si]62N3[Si]51N64 HQVNEWCFYHHQES-UHFFFAOYSA-N 0.000 title claims description 81
- 238000004519 manufacturing process Methods 0.000 title claims description 13
- 238000000034 method Methods 0.000 title description 33
- 239000007789 gas Substances 0.000 claims description 32
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 claims description 29
- 238000005121 nitriding Methods 0.000 claims description 29
- 229910052751 metal Inorganic materials 0.000 claims description 24
- 239000002184 metal Substances 0.000 claims description 24
- 239000011863 silicon-based powder Substances 0.000 claims description 21
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 18
- 150000004820 halides Chemical class 0.000 claims description 11
- 229910052757 nitrogen Inorganic materials 0.000 claims description 9
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims description 8
- 229910001508 alkali metal halide Inorganic materials 0.000 claims description 5
- 150000008045 alkali metal halides Chemical class 0.000 claims description 4
- 229910001615 alkaline earth metal halide Inorganic materials 0.000 claims description 4
- 229910021529 ammonia Inorganic materials 0.000 claims description 4
- 239000000843 powder Substances 0.000 description 91
- 239000001301 oxygen Substances 0.000 description 42
- 229910052760 oxygen Inorganic materials 0.000 description 42
- 238000005245 sintering Methods 0.000 description 42
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 40
- 239000013078 crystal Substances 0.000 description 25
- 238000006243 chemical reaction Methods 0.000 description 24
- 239000002245 particle Substances 0.000 description 21
- 230000000052 comparative effect Effects 0.000 description 18
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 16
- 239000012071 phase Substances 0.000 description 14
- 239000000203 mixture Substances 0.000 description 13
- 229910052710 silicon Inorganic materials 0.000 description 13
- 239000010703 silicon Substances 0.000 description 13
- 239000012535 impurity Substances 0.000 description 11
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 10
- 239000000395 magnesium oxide Substances 0.000 description 10
- 238000000465 moulding Methods 0.000 description 8
- 229910004261 CaF 2 Inorganic materials 0.000 description 7
- 239000002994 raw material Substances 0.000 description 7
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 6
- 238000005452 bending Methods 0.000 description 6
- 229910052791 calcium Inorganic materials 0.000 description 6
- 238000011161 development Methods 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- 239000007791 liquid phase Substances 0.000 description 6
- 238000010298 pulverizing process Methods 0.000 description 6
- 150000001340 alkali metals Chemical class 0.000 description 5
- 230000015572 biosynthetic process Effects 0.000 description 5
- 229910052736 halogen Inorganic materials 0.000 description 5
- 150000002367 halogens Chemical class 0.000 description 5
- 229910001404 rare earth metal oxide Inorganic materials 0.000 description 5
- 239000007787 solid Substances 0.000 description 5
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 4
- 229910052783 alkali metal Inorganic materials 0.000 description 4
- 239000011777 magnesium Substances 0.000 description 4
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 description 4
- 230000007704 transition Effects 0.000 description 4
- 229910052782 aluminium Inorganic materials 0.000 description 3
- 150000001875 compounds Chemical class 0.000 description 3
- 238000005090 crystal field Methods 0.000 description 3
- 229910052742 iron Inorganic materials 0.000 description 3
- 230000006911 nucleation Effects 0.000 description 3
- 238000010899 nucleation Methods 0.000 description 3
- 239000002243 precursor Substances 0.000 description 3
- 238000001272 pressureless sintering Methods 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 239000000377 silicon dioxide Substances 0.000 description 3
- -1 silicon halide Chemical class 0.000 description 3
- KRHYYFGTRYWZRS-UHFFFAOYSA-N Fluorane Chemical compound F KRHYYFGTRYWZRS-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 description 2
- 229910052784 alkaline earth metal Inorganic materials 0.000 description 2
- 150000001342 alkaline earth metals Chemical class 0.000 description 2
- 238000013459 approach Methods 0.000 description 2
- 229910052786 argon Inorganic materials 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000011049 filling Methods 0.000 description 2
- 238000010304 firing Methods 0.000 description 2
- 150000002222 fluorine compounds Chemical class 0.000 description 2
- 238000005469 granulation Methods 0.000 description 2
- 230000003179 granulation Effects 0.000 description 2
- 230000005764 inhibitory process Effects 0.000 description 2
- 238000001746 injection moulding Methods 0.000 description 2
- 229910052744 lithium Inorganic materials 0.000 description 2
- 229910052749 magnesium Inorganic materials 0.000 description 2
- YIXJRHPUWRPCBB-UHFFFAOYSA-N magnesium nitrate Chemical compound [Mg+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O YIXJRHPUWRPCBB-UHFFFAOYSA-N 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000013001 point bending Methods 0.000 description 2
- 238000007569 slipcasting Methods 0.000 description 2
- 238000001238 wet grinding Methods 0.000 description 2
- UOCLXMDMGBRAIB-UHFFFAOYSA-N 1,1,1-trichloroethane Chemical compound CC(Cl)(Cl)Cl UOCLXMDMGBRAIB-UHFFFAOYSA-N 0.000 description 1
- 238000007088 Archimedes method Methods 0.000 description 1
- 229910000882 Ca alloy Inorganic materials 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 229910052684 Cerium Inorganic materials 0.000 description 1
- 229910052693 Europium Inorganic materials 0.000 description 1
- 229910052772 Samarium Inorganic materials 0.000 description 1
- 230000002159 abnormal effect Effects 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000010306 acid treatment Methods 0.000 description 1
- 229910052788 barium Inorganic materials 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- 150000001649 bromium compounds Chemical class 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 238000003889 chemical engineering Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 150000001805 chlorine compounds Chemical class 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000000280 densification Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 230000001747 exhibiting effect Effects 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 229910052746 lanthanum Inorganic materials 0.000 description 1
- ZLNQQNXFFQJAID-UHFFFAOYSA-L magnesium carbonate Chemical compound [Mg+2].[O-]C([O-])=O ZLNQQNXFFQJAID-UHFFFAOYSA-L 0.000 description 1
- 239000001095 magnesium carbonate Substances 0.000 description 1
- 229910000021 magnesium carbonate Inorganic materials 0.000 description 1
- VTHJTEIRLNZDEV-UHFFFAOYSA-L magnesium dihydroxide Chemical compound [OH-].[OH-].[Mg+2] VTHJTEIRLNZDEV-UHFFFAOYSA-L 0.000 description 1
- 239000000347 magnesium hydroxide Substances 0.000 description 1
- 229910001862 magnesium hydroxide Inorganic materials 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 239000011812 mixed powder Substances 0.000 description 1
- 229910000480 nickel oxide Inorganic materials 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 1
- SIWVEOZUMHYXCS-UHFFFAOYSA-N oxo(oxoyttriooxy)yttrium Chemical compound O=[Y]O[Y]=O SIWVEOZUMHYXCS-UHFFFAOYSA-N 0.000 description 1
- GNRSAWUEBMWBQH-UHFFFAOYSA-N oxonickel Chemical compound [Ni]=O GNRSAWUEBMWBQH-UHFFFAOYSA-N 0.000 description 1
- 150000002926 oxygen Chemical class 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
- 229910052712 strontium Inorganic materials 0.000 description 1
- 238000000859 sublimation Methods 0.000 description 1
- 230000008022 sublimation Effects 0.000 description 1
- 230000002194 synthesizing effect Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 229910052727 yttrium Inorganic materials 0.000 description 1
- 239000011787 zinc oxide Substances 0.000 description 1
Landscapes
- Ceramic Products (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は高温強度の大きな焼結体を製造することができ
る窒化ケイ素の製造方法に関する。窒化ケイ素は高温構
造材料としてガスタービン部材、ノズル、軸受等に利用
されている。The present invention relates to a method for producing silicon nitride capable of producing a sintered body having high strength at high temperature. Silicon nitride is used as a high temperature structural material for gas turbine members, nozzles, bearings and the like.
〔従来の技術〕 従来、窒化ケイ素粉末の製法としては、(1)金属ケイ
素直接窒化法、(2)シリカ還元窒化法、(3)ハロゲ
ン化ケイ素法が知られている。これらの方法でつくられ
る粉末は、製造履歴が異なるためか、金属不純物量や酸
素量あるいは粒径、比表面積が同程度であつても、粉末
の焼結性や焼結後の焼結体の特性例えば曲げ強度に大き
な違いがある。[Prior Art] Conventionally, as methods for producing silicon nitride powder, (1) metal silicon direct nitriding method, (2) silica reduction nitriding method, and (3) silicon halide method are known. Probably because the powders produced by these methods have different manufacturing histories, even if the amount of metal impurities, the amount of oxygen, the particle size, and the specific surface area are the same, the sinterability of the powder and the sintered body after sintering are There is a big difference in characteristics such as bending strength.
一般的には、(1)の方法で製造された粉末は易焼結性
であるが高温曲げ強度が低い(2)の方法の粉末は難焼
結性であるが高温曲げ強度が高い、(3)の方法の粉末
は中間的な性能を示すといわれている。Generally, the powder produced by the method (1) is easily sinterable but has low high-temperature bending strength. The powder of the method (2) is hardly sinterable but has high high-temperature bending strength. The powder of method 3) is said to exhibit intermediate performance.
酸素量については、(1)の方法の粉末は粉砕工程を経
るため通常全酸素量が2重量%を超える場合が多く少な
くとも1.5重量%はある。(1)の方法で不純物除去の
ために酸処理等の工程を通すと全酸素量は低減するがそ
れでも1.0重量%未満にすることは難しい。一方、
(2)の方法の粉末でも、原料としてシリカ粉末を用い
るためにシリカの残留があり、全酸素量は2重量%を超
えるのが普通である。Regarding the amount of oxygen, since the powder of the method (1) undergoes a pulverization step, the total amount of oxygen is usually more than 2% by weight in most cases and is at least 1.5% by weight. If the method of (1) is passed through a step such as an acid treatment for removing impurities, the total oxygen amount is reduced, but it is still difficult to reduce it to less than 1.0% by weight. on the other hand,
Even in the case of the powder of the method (2), since silica powder is used as a raw material, there is residual silica, and the total amount of oxygen usually exceeds 2% by weight.
以上の粉末が現状入手可能なものである。当然のことな
がら、粉末の焼結性及び焼結体特性には粉末酸素量の影
響があるのはもちろんであるが、その他に比表面積、結
晶性、粒子形状、粒度(微粉)等様々の粉体特性がから
みあつており、前記各製法の粉末特性が粉体特性にどの
ように関係しているかはほとんどわかつていないのが現
状である。The above powders are currently available. Needless to say, the sinterability of the powder and the characteristics of the sintered body are affected by the amount of powder oxygen, but in addition, various powders such as specific surface area, crystallinity, particle shape, and particle size (fine powder) are also included. At present, the body characteristics are entangled, and it is hardly known how the powder characteristics of the above-mentioned production methods are related to the powder characteristics.
特公昭61−43311号公報には、窒化ケイ素粉末の酸素量
と高温曲げ強度との関係が記載されている。Japanese Examined Patent Publication No. 61-43311 discloses the relationship between the oxygen content of silicon nitride powder and high-temperature bending strength.
しかし、上記発明は窒化ケイ素粉末の酸素量を少なくし
高温強度に優れた焼結体を提案しているが、HP焼結方法
を採用しているためか、酸素以外の諸特性例えば塊であ
るインゴツトを粉砕する方法では不可避な微粉量、金属
不純物、比表面積等の記載が明確化されていないこと、
低酸素粉末の製造方法において、特殊処理を施している
ことからくるコスト高、焼結方法が前述したように汎用
性の薄いHPを採用していること、更には何故高温強度が
発現したかに係る焼結助剤種の限定理由及び焼結体の組
織については深く言及していない。However, the above-mentioned invention proposes a sintered body which has a reduced amount of oxygen in silicon nitride powder and is excellent in high-temperature strength. However, because of adopting the HP sintering method, various characteristics other than oxygen, for example, a lump. In the method of crushing the ingot, the amount of fine powder unavoidable, the description of metal impurities, specific surface area, etc. are not clarified,
In the method of producing low oxygen powder, the cost is high due to the special treatment, the versatile HP is used for the sintering method as described above, and the reason why the high temperature strength is exhibited The reason for limiting the type of the sintering aid and the structure of the sintered body are not mentioned deeply.
本発明の目的は、前記課題を解決した窒化ケイ素の製造
方法を提供することにある。An object of the present invention is to provide a method for manufacturing silicon nitride that solves the above problems.
本発明を概説すれば、本発明は窒化ケイ素の製造方法に
関する発明であつて、窒素及び/又はアンモニアを含む
雰囲気中で金属ケイ素粉末を窒化して窒化ケイ素を製造
する方法において、アルカリ金属ハロゲン化物及びアル
カリ土類金属ハロゲン化物よりなる群から選択したハロ
ゲン化物の少なくとも1種を、気体の状態で連続的、間
欠的又は一時的に供給することを特徴とする。Briefly describing the present invention, the present invention relates to a method for producing silicon nitride, which comprises nitriding a metal silicon powder in an atmosphere containing nitrogen and / or ammonia to produce silicon nitride. And at least one kind of halide selected from the group consisting of alkaline earth metal halides is continuously, intermittently or temporarily supplied in a gaseous state.
本発明者らは前記の点について種々検討した結果、金属
ケイ素粉末を特殊な雰囲気ガス下で窒化することによ
り、窒化ケイ素粉末の酸素量、比表面積、平均粒子径、
微粉量及び金属不純物を制御した粉末を製造すると共
に、該窒化ケイ素粉末となじみの良い焼結助剤を見出
し、更に、その焼結体の高温強度発現に大きく寄与する
組織も見出し、本発明を完成した。As a result of various studies on the above points, the inventors of the present invention nitriding the metal silicon powder under a special atmosphere gas, the oxygen content of the silicon nitride powder, the specific surface area, the average particle diameter,
Along with producing a powder in which the amount of fine powder and metal impurities are controlled, a sintering aid that is well compatible with the silicon nitride powder is found, and a structure that greatly contributes to the high temperature strength development of the sintered body is also found, and the present invention is provided. completed.
本発明における窒化ケイ素粉末の酸素は0.6重量%以
下、好ましくは0.6重量%から0.2重量%である。酸素を
0.6重量%以下に限定したのはそれよりも多いと焼結の
際に生じるα→β転移が低温から起こりやすくなり、更
には焼結助剤が形成する粒界相の量が多くなるので窒化
ケイ素への溶解性が大きくなり、その結果、β核の数が
多くなり、充分に成長したアスペクト比の高いβ柱状晶
を得ることが困難となるからである。The oxygen content of the silicon nitride powder in the present invention is 0.6% by weight or less, preferably 0.6% by weight to 0.2% by weight. Oxygen
If the content is more than 0.6% by weight, the α → β transition that occurs during sintering tends to occur from low temperature, and the amount of grain boundary phase formed by the sintering aid increases, so the nitriding is limited. This is because the solubility in silicon increases, and as a result, the number of β nuclei increases and it becomes difficult to obtain a sufficiently grown β columnar crystal having a high aspect ratio.
平均粒子径は特に常圧焼結を採用する場合、非常に重要
であり一般的には小さいことが好ましいと言われてい
る。本発明の平均粒子径は0.3〜0.8μmの範囲である。
0.8μmを越えると、焼結助剤例えば酸化イツトリウ
ム、酸化マグネシウム、酸化アルミニウム等と窒化ケイ
素粉末中に含まれる酸素との反応により生じる複合酸化
物への窒化ケイ素の溶解度の低下が起こり充分にち密化
しなくなるからである。0.3μm未満であると焼結助剤
が形成する粒界相への溶解度が大きくなり、その結果、
β核の数が多くなり、充分にち密化しなくなり、高温で
十分耐えるような焼結体が常圧焼結では得られ難くなる
からである。It is said that the average particle size is very important especially when adopting pressureless sintering, and it is generally preferable that the average particle size is small. The average particle diameter of the present invention is in the range of 0.3 to 0.8 μm.
If it exceeds 0.8 μm, the solubility of silicon nitride in the composite oxide caused by the reaction of sintering aids such as yttrium oxide, magnesium oxide, aluminum oxide, etc. with oxygen contained in the silicon nitride powder will decrease, and the density will be sufficiently dense. Because it does not change. If it is less than 0.3 μm, the solubility in the grain boundary phase formed by the sintering aid becomes large, and as a result,
This is because the number of β nuclei becomes large, the densification does not become sufficiently dense, and it becomes difficult to obtain a sintered body that can withstand high temperature sufficiently by pressureless sintering.
なお、本発明で用いている平均粒子径とは堀場製作所製
のCAPA−700で測定した体積%の50%径のことである。The average particle diameter used in the present invention is the 50% diameter of the volume% measured by CAPA-700 manufactured by Horiba Ltd.
一般に、窒化ケイ素粉末中の酸素が少なくなると、一般
的な焼結助剤Y2O3、Al2O3系では、S.H.ハンプシヤ及び
K.H.ジヤツク〔S.H.Hampshire、K.H.Jack、プロシーデ
イングス オブ ブリテイツシユ セラミツク ソサイ
エテイ(Proc.Brit.Ceram.Soc)第31巻、第37〜49頁(1
981)〕らが述べているように、液相量が十分に得られ
ないため、焼結しづらくなる傾向にある。すなわち、相
境界反応律速となり、一般には拡散を速める効果のある
焼結助剤例えばMgOを添加し焼結する。その場合焼結性
は改善されるが、前述したようなアスペクト比の高いβ
柱状晶に問題が残る。つまり、特願昭63−277360号明細
書に述べているような微粉量にアスペクト比の高いβ柱
状晶が大きく影響することである。すなわち、微粉量が
多くなると、液相中に生じるβ核の数が多くなるためか
アスペクト比の高いβ柱状晶が生じ難くなり、結果とし
て、高温強度が発現しなくなる。In general, when the oxygen content in the silicon nitride powder is low, the SH hump shear and the general sintering aids Y 2 O 3 and Al 2 O 3 are used.
KH Jack (SHHampshire, KHJack, Proceedings of British Ceramic Society, Proc.Brit.Ceram.Soc, Vol. 31, pp. 37-49 (1
981)] et al., It is difficult to sinter because a sufficient amount of liquid phase cannot be obtained. That is, the phase boundary reaction is rate-determining, and generally, a sintering aid, such as MgO, which has an effect of accelerating diffusion is added and sintered. In that case, the sinterability is improved, but the high aspect ratio β
The problem remains in columnar crystals. That is, the β columnar crystals having a high aspect ratio greatly affect the amount of fine powder as described in Japanese Patent Application No. 63-277360. That is, when the amount of fine powder increases, β columnar crystals having a high aspect ratio are less likely to occur, probably because the number of β nuclei generated in the liquid phase increases, and as a result, high temperature strength does not develop.
すなわち、微粉量としては特願昭63−277360号明細書に
記載しているように0.2μm以下の微粉量を規定した場
合、7容量%以下が好ましい。また、換言すれば相境界
反応律速を助けるような焼結助剤を加えて焼結し、十分
焼結密度がアツプし、且つアスペクト比の高いβ柱状晶
が晶出していること、つまり、焼結体特性としては高温
強度(σ1200℃)が700MPa以上発現することである。こ
のような焼結助剤としては、MgO系、MgO−Al2O3系、MgO
−希土類元素酸化物系、MgO−Al2O3−希土類元素酸化物
系、MgO・Al2O3−希土類元素酸化物系が挙げられる。That is, the amount of fine powder is preferably 7% by volume or less when the amount of fine powder is 0.2 μm or less as described in Japanese Patent Application No. 63-277360. In other words, sintering is performed by adding a sintering aid that helps control the phase boundary reaction, and the β-columnar crystals with a sufficiently high sintering density and high aspect ratio are crystallized, that is, firing. The binding property is that the high temperature strength (σ 1200 ° C ) is 700 MPa or more. As such a sintering aid, MgO-based, MgO-Al 2 O 3 system, MgO
- rare earth oxide-based, MgO-Al 2 O 3 - rare earth oxide-based, MgO · Al 2 O 3 - include rare earth oxide.
なお、前述した焼結体中のアスペクト比の高いβ柱状晶
と高温強度の関係については後で詳細に述べるが、今
回、見出したことはアスペクト比の高いβ柱状晶が高温
強度発現に大きな役割をしていることである。The relationship between the β-columnar crystals with a high aspect ratio and the high temperature strength in the above-mentioned sintered body will be described in detail later. That is.
また、α分率は上述してきたように窒化ケイ素の焼結機
構はα−窒化ケイ素が一度液相に溶解し、その後過飽和
となりβ−窒化ケイ素として析出することが基本となつ
ているので、窒化ケイ素粉末中のα相含有率は高いこと
が望ましい。すなわちα相含有率は少なくとも80%以上
存在することが必要である。80%未満であると前述した
アスペクト比の高いβ柱状晶が晶出し難くなり高温強度
発現に結びつかなくなるからである。In addition, the α fraction is based on the fact that the sintering mechanism of silicon nitride is based on the fact that α-silicon nitride is once dissolved in the liquid phase, then becomes supersaturated and precipitates as β-silicon nitride, as described above. It is desirable that the α-phase content in the silicon powder is high. That is, the α phase content must be at least 80% or more. If it is less than 80%, the above-mentioned β columnar crystals having a high aspect ratio are hard to crystallize and the high temperature strength is not exhibited.
窒化ケイ素粉末中の金属不純物含有量、とりわけFe、Al
及びCaの含有量の合計は500ppm以下であることが好まし
い。500ppmを越えると高温下で、長期にわたり使用した
場合、すなわち、高温でのクリープ強度が低下するから
である。したがつて、金属不純物はできるだけ少ない方
が好ましい。Content of metal impurities in silicon nitride powder, especially Fe, Al
The total content of Ca and Ca is preferably 500 ppm or less. This is because if it exceeds 500 ppm, the creep strength at a high temperature is prolonged, that is, the creep strength at a high temperature is lowered. Therefore, it is preferable that the metal impurities are as small as possible.
また、比表面積については、各種成形方法例えばプレス
成形、射出成形、スリツプキヤスト等を用いて形を作る
場合、ハンドリング、粘性等の理由から一般的には6〜
14m2/gであることが好ましい。6m2/g未満であると、粒
度が粗くなり、結果として焼結性が悪くなり好ましくな
い。14m2/gを越えると粉末自身カサ高となり、ハンドリ
ングが悪くなつたり、射出成形性にとつて重要な要素と
なつている粘性が高くなり、好ましくない。Regarding the specific surface area, when a shape is formed by using various molding methods such as press molding, injection molding, slip casting, etc., it is generally 6 to 6 for reasons such as handling and viscosity.
It is preferably 14 m 2 / g. When it is less than 6 m 2 / g, the grain size becomes coarse, and as a result, the sinterability is deteriorated, which is not preferable. If it exceeds 14 m 2 / g, the powder itself becomes bulky, resulting in poor handling and high viscosity, which is an important factor for injection moldability, which is not preferable.
更に付け加えるならば6m2/g未満であると粒子が大きく
なり、焼結密度が上がらず、高温強度が向上につながら
ない。また、14m2/gを越えるためには過粉砕を要し、そ
の結果微粉量が多くなり、前述したようにβ核の数が多
くなり、アスペクト比の高いβ柱状晶が生じ難くなるか
らである。In addition, if it is less than 6 m 2 / g, the particles become large, the sintering density does not increase, and the high temperature strength cannot be improved. Further, in order to exceed 14 m 2 / g, excessive pulverization is required, and as a result, the amount of fine powder increases, the number of β nuclei increases as described above, and β columnar crystals with a high aspect ratio are less likely to occur. is there.
次に、上記説明した窒化ケイ素の製造方法について述べ
る。Next, a method for manufacturing the above-described silicon nitride will be described.
本発明の窒化ケイ素は窒素及び又はアンモニアを含む雰
囲気ガスを導入しながら、金属ケイ素粉末を窒化して、
窒化ケイ素を製造する方法において、アルカリ金属及び
アルカリ類金属の各ハロゲン化物から選ばれた1種又は
2種以上を気体の状態で連続的、間欠的又は一時的に供
給することにより製造される。Silicon nitride of the present invention, while introducing an atmosphere gas containing nitrogen and or ammonia, by nitriding the metal silicon powder,
In the method for producing silicon nitride, it is produced by continuously, intermittently or temporarily supplying one or more selected from alkali metal and alkali metal halides in a gaseous state.
以下、更に詳しく本発明について説明する。Hereinafter, the present invention will be described in more detail.
本発明で使用する金属ケイ素粉末の粒度は88μm下が好
ましい。このように、比較的粒度の大きな金属ケイ素を
用いることができる理由は、後述のように、金属ケイ素
と窒素源との反応のすべてが固・気反応ではなく、表面
の若干の固・気反応後は気・気反応で窒化が進むことに
大きく関与している。すなわち、本発明では、たとえ88
μm程度の金属ケイ素であつても表面の一部が、固・気
反応により窒化が起きれば、金属ケイ素とα−窒化ケイ
素の密度差により金属ケイ素の破壊現象が生じ微細な金
属ケイ素となるからである。しかし、88μmを越える
と、同様な現象が生じるが、表面の固・気反応の生じる
温度が高くなり、通常の窒化条件では遊離のSiが残りや
すくなり好ましくはない。下限値については特に制限は
ない。つまり、平均粒子径の小さな金属ケイ素粉末を用
いれば用いる程、後述するSiO(G)が生成しやすくな
り気・気反応が促進されるので目的とする粒状化α−窒
化ケイ素インゴツトを製造しやすくなる。また、金属ケ
イ素粉末中の酸素は上述した窒化ケイ素粉末のところで
詳細に述べたように低酸素化を目的としているので、な
るべく金属ケイ素粉末中の酸素は少ないことが望まし
い。本発明においては0.2%以下であれば良い。The particle size of the metallic silicon powder used in the present invention is preferably under 88 μm. As described below, the reason why metallic silicon having a relatively large particle size can be used is that all the reactions between metallic silicon and the nitrogen source are not solid / gas reactions, but rather some solid / gas reactions on the surface. After that, it is greatly involved in the progress of nitriding by the gas-gas reaction. That is, in the present invention, even if
Even with metallic silicon of about μm, if part of the surface undergoes nitriding due to solid-gas reaction, the density difference between metallic silicon and α-silicon nitride causes a phenomenon of breaking metallic silicon, resulting in fine metallic silicon. Is. However, if it exceeds 88 μm, the same phenomenon occurs, but the temperature at which the solid-gas reaction occurs on the surface becomes high, and free Si tends to remain under normal nitriding conditions, which is not preferable. There is no particular lower limit. In other words, the use of metallic silicon powder having a smaller average particle size facilitates the production of SiO (G) described later and promotes the gas-gas reaction, which makes it easier to produce the target granular α-silicon nitride ingot. Become. Further, since the oxygen in the metal silicon powder is aimed at lowering the oxygen level as described in detail in the above-mentioned silicon nitride powder, it is desirable that the oxygen content in the metal silicon powder is as small as possible. In the present invention, it may be 0.2% or less.
以上のように、本発明は特願昭63−198987号明細書にお
ける金属ケイ素粉末から窒化ケイ素が生成する反応機構
の応用にある。すなわち、金属ケイ素粉末と窒素との反
応は固・気反応よりむしろ、O2を介したN2−NH3又はN2
−H2系の気・気反応に律速されていることを知ると共
に、SiO(G)の関与したSi3N4生成の反応式を種々検討
した。この1例を下記に示すが、このような気・気反応
による固体生成における形態については加藤〔加藤昭
夫:粉体工学会誌、第18巻、第1号、第36〜45頁(198
0)〕が述べているように過飽和度、すなわちlogkpに大
きく影響する。つまり、下記(1)式の1300℃でのlogk
pは1.6程度であるのに対し、(2)式は46程度となる。As described above, the present invention lies in the application of the reaction mechanism for producing silicon nitride from metallic silicon powder in Japanese Patent Application No. 63-198987. Ie, the reaction of a metal silicon powder and nitrogen rather than solid-gas reaction, N 2 -NH 3, or N 2 through the O 2
While knowing that the -H 2 system is rate-controlled by the gas-gas reaction, various reaction equations for Si 3 N 4 formation involving SiO (G) were investigated. One example of this is shown below, but regarding the morphology in solid formation by such a gas-gas reaction, Kato [Akio Kato: Journal of Powder Engineering, Vol. 18, No. 1, pp. 36-45 (198
0)] has a great influence on the degree of supersaturation, that is, logkp. That is, the logk at 1300 ° C in the following equation (1)
While p is about 1.6, Equation (2) is about 46.
したがつて、この両式下より生成される窒化ケイ素の形
態は(1)式のウイスカー、(2)式が粒状を呈するの
ではないかと推定される。Therefore, it is presumed that the morphology of silicon nitride produced by the above two equations may be the whiskers of the equation (1) and the granularity of the equation (2).
3SiO(G)+4NH3(G) =Si3N4(S)+3/2 O2(G)+6H2(G) (1) 3Si(G)+4NH3(G) =Si3N4(S)+6H2(G) (2) また、Si(G)が生じるまでの反応式をCaF2(G)を例
にとり、推定した反応、並びにそのミクロ的結晶場にお
ける循環反応を式(3)〜(6)に示す。3SiO (G) + 4NH 3 (G) = Si 3 N 4 (S) + 3/2 O 2 (G) + 6H 2 (G) (1) 3Si (G) + 4NH 3 (G) = Si 3 N 4 (S) + 6H 2 (G) (2) In addition, taking the reaction equation up to the formation of Si (G) by taking CaF 2 (G) as an example, the estimated reaction and the circulating reaction in the microscopic crystal field are expressed by equations (3) to ( 6).
Si(S)+1/2 O2(G)→SiO(G) (3) SiO(G)+CaF2(G)+H2(G) →Si(G)+CaO(S)+2HF(G) (4) 3Si(G)+4NH3(G)→Si3N4(S)+6H2(G)
(5) (CaO(S)+2HF(G) →CaF2(G)+H2(G)+1/2 O2(G)) (6) これからも明らかなように気体として同伴されたハロゲ
ン化物の気体はミクロ的結晶場において循環している可
能性も考えられる。事実、当量以下のハロゲン化物の気
体でも十分に粒状化の効果が認められた。Si (S) +1/2 O 2 (G) → SiO (G) (3) SiO (G) + CaF 2 (G) + H 2 (G) → Si (G) + CaO (S) + 2HF (G) (4) 3Si (G) + 4NH 3 (G) → Si 3 N 4 (S) + 6H 2 (G)
(5) (CaO (S) + 2HF (G) → CaF 2 (G) + H 2 (G) +1/2 O 2 (G)) (6) As is clear from this, halide gas entrained as a gas It is possible that is circulating in the microscopic crystal field. In fact, even if the amount of the halide gas is not more than the equivalent amount, the effect of the granulation is sufficiently recognized.
そこで、SiO(G)より更に酸素との親和性の強い気体
化合物の探索を行つた。その結果、窒素及び/又はアン
モニアを含む雰囲気ガスを導入しながら、金属ケイ素粉
末を窒化するに際し、アルカリ金属及びアルカリ土類金
属の各ハロゲン化物の気体を意図的に供給すれば生成す
る窒化ケイ素の形態がウイスカー状ではなく粒状になる
ことを見出した。アルカリ金属及びアルカリ土類金属の
ハロゲン化物の濃度については、例えば前述した推定反
応式からもわかるように、Si(S)1molに対し、アルカ
リ土類金属のハロゲン化物の気体であれば1mol、また、
アルカリ金属のハロゲン化物であれば2mol以上あれば十
分である。また、窒化は一度に行われないので、実際は
それ以下で良い。供給方法については例えば別な炉の中
にアルカリ金属及びアルカリ土類金属のハロゲン化物を
装入し、加熱昇華し、金属ケイ素粉末が装入されている
炉の中へ、濃度を規定しながら窒素同伴で供給する。ま
た、金属ケイ素粉末が装入されている炉の中に前記ハロ
ゲン化物は金属ケイ素粉末の近傍に規定量置き、金属ケ
イ素粉末の窒化・前記ハロゲン化物の昇華を行う形で供
給することもできる。供給方法についてはこれらに限ら
れたものではない。また、導入形式についてもこれに限
られたものではなく、別々導入、同一混合導入のいずれ
でもかまわない。Therefore, we searched for a gas compound that has a stronger affinity for oxygen than SiO (G). As a result, when nitriding the metal silicon powder while introducing an atmosphere gas containing nitrogen and / or ammonia, the gas of each halide of alkali metal and alkaline earth metal is intentionally supplied to generate silicon nitride. It was found that the morphology was granular, not whisker-like. Regarding the concentration of alkali metal and alkaline earth metal halides, for example, as can be seen from the above-mentioned estimated reaction formula, 1 mol of Si (S) is 1 mol of gas of alkaline earth metal halide, and ,
If it is an alkali metal halide, 2 mol or more is sufficient. In addition, since nitriding is not performed at one time, it may actually be less than that. Regarding the supply method, for example, a halide of an alkali metal and an alkaline earth metal is charged into another furnace, heated and sublimated, and nitrogen is supplied to a furnace charged with metallic silicon powder while controlling the concentration. Supplied as a companion. It is also possible to place a specified amount of the halide in the vicinity of the metal silicon powder in a furnace charged with the metal silicon powder, and supply the metal silicon powder by nitriding the metal silicon powder and sublimating the halide. The supply method is not limited to these. Further, the introduction form is not limited to this, and may be either separate introduction or the same mixed introduction.
更に、供給時期としては、窒化が行われている温度、す
なわち、1,150℃から1,450℃の範囲の温度において、連
続的、間欠的又は一時的に供給する。この一時供給につ
いては例えば前述した昇華を行う炉と窒化を行う炉への
導入配管の開閉を組合せ操作することにより達成され
る。Further, as the supply timing, the nitriding is performed at a temperature, that is, a temperature in the range of 1,150 ° C. to 1,450 ° C., continuously, intermittently or temporarily. This temporary supply can be achieved by, for example, performing a combined operation of opening and closing the introduction pipes to the above-mentioned furnace for sublimation and the furnace for nitriding.
この一時的な供給の裏付けについてはミクロ的結晶場に
おいて、例えば下記に示すように導入された気体の前記
ハロゲン化物が系内に循環されているからと理解してい
る。実際、温度で言えば1,350℃まで前記ハロゲン化物
を導入し、その後前記気体の供給を止めても生成する窒
化ケイ素の形態は1,450℃まで導入し続けたものと変ら
なかつた。It is understood that this temporary supply is supported by the fact that the introduced gas halide is circulated in the system in the microscopic crystal field, for example, as shown below. In fact, in terms of temperature, even if the halide was introduced up to 1,350 ° C., and then the supply of the gas was stopped, the form of silicon nitride formed was still the same as that continued to 1,450 ° C.
前述したアルカリ金属及びアルカリ金属のハロゲン化物
は例えばLi、Na、K、Mg、Ca、Sr、Ba元素のフツ化物、
塩化物、臭化物である。特にCa、Mg、Liのフツ化物が好
ましい。その理由としては、酸化物生成の標準生成エネ
ルギーと温度の関係においてSiより酸素との親和性が強
いからであり、その結果として前述した粒状化が一層促
進されるからである。The above-mentioned alkali metal and alkali metal halide are, for example, fluorides of Li, Na, K, Mg, Ca, Sr, and Ba elements,
Chlorides and bromides. Particularly, fluorides of Ca, Mg and Li are preferable. The reason is that the affinity for oxygen is stronger than that of Si in the relationship between the standard formation energy of oxide formation and the temperature, and as a result, the above-mentioned granulation is further promoted.
また、前記ハロゲン化物は単独で用いても良いし、2種
以上のものを併用しても差支えない。更に付け加えるな
らば窒化炉にも限定されるものではない。例えばバツチ
炉、連続プツシヤー炉、連続回転炉、連続スクリユー
炉、流動層いずれにも応用可能である。The above halides may be used alone or in combination of two or more kinds. If it adds further, it is not limited to a nitriding furnace. For example, it can be applied to any of a batch furnace, a continuous push furnace, a continuous rotary furnace, a continuous screen furnace, and a fluidized bed.
以上説明した粒状化窒化ケイ素及び特願昭63−198987号
明細書に記載したところのウイスカー状の窒化ケイ素の
具体例を第1図及び第2図に示す。また第3図にはSiの
直接窒化法で得られる典型的な固・気反応の例、つまり
他形を呈する形態を示す。なお各図は倍率3500倍の走査
型電子顕微鏡(SEM)写真である。Specific examples of the granular silicon nitride described above and the whisker-like silicon nitride described in Japanese Patent Application No. 63-198987 are shown in FIGS. 1 and 2. Further, FIG. 3 shows an example of a typical solid-gas reaction obtained by the direct nitriding method of Si, that is, a form exhibiting another shape. Each figure is a scanning electron microscope (SEM) photograph at a magnification of 3500 times.
これからも明らかなように、第1図は用いたSi粉末より
数段に小さく、かつ丸味を帯びた粒状を呈していること
がわかると共に、気・気反応が生じたことも裏付けられ
る。As is clear from this, it can be seen that FIG. 1 is much smaller than the Si powder used and has a roundish granular shape, and also supports the occurrence of the qi-qi reaction.
第2図も気・気反応が生じたことは明らかであるが、Si
O(G)の過飽和度不足のためか、針状晶の多い形態と
なつている。第3図は、まずSi粉末同士の焼結が起こ
り、その後、窒素が拡散し、窒化が進んだ形跡が如実に
わかる。It is clear that Qi-Qi reaction also occurred in Fig. 2, but Si
Maybe due to lack of supersaturation of O (G), it is in a form with many needle crystals. In FIG. 3, it can be clearly seen that the sintering of the Si powders first occurs, and then the nitrogen diffuses and the nitriding proceeds.
このような粒状化した窒化ケイ素は粉砕される際に微粉
が生じ難くなると共に、その結果、低酸素化にもつなが
り、本発明の目的である低酸素且つ微粉の少ない窒化ケ
イ素粉末を容易に製造することができる。Such granulated silicon nitride makes it difficult to generate fine powder when pulverized, and as a result, it also leads to low oxygen, and easily manufactures the low-oxygen and low-fine silicon nitride powder which is the object of the present invention. can do.
ここで、本発明によつて得られた粒状化窒化ケイ素につ
いて更に詳しく説明すると、第2図に示すような径の細
いウイスカー又は針状晶を物理的に抗折しながら粉砕す
るのではなく、第1図のような粒状晶をほぐす形で粉砕
が進むので、インゴツトの粉砕に伴う微粉の発生が少な
く、その結果窒化ケイ素の酸化が抑制され、低酸素粉末
となる。すなわち、ハロゲン化ケイ素法で得られるよう
な微粉のない等軸の粉体に近い窒化ケイ素粉末となる。
定量的には通常の粗砕機と中砕機を用いて粗砕・中砕物
に粉砕したとき、その粗・中砕物特に粒子径0.2mm下の
比表面積が2〜5m2/gとなるように窒化ケイ素でありか
つ酸素含有量が0.4%以下となるような窒化ケイ素であ
る。Here, the granular silicon nitride obtained according to the present invention will be described in more detail. Rather than crushing whiskers or needle-shaped crystals having a small diameter as shown in FIG. 2 while physically bending, Since the pulverization proceeds in such a manner as to loosen the granular crystals as shown in FIG. 1, the generation of fine powder due to the pulverization of the ingot is small, and as a result, the oxidation of silicon nitride is suppressed, resulting in a low oxygen powder. That is, it becomes a silicon nitride powder close to equiaxed powder without fine powder as obtained by the silicon halide method.
Quantitatively, when crushed into coarse / medium crushed products using an ordinary coarse crusher and medium crusher, the coarse / medium crushed products, especially nitriding so that the specific surface area with a particle diameter of 0.2 mm is 2 to 5 m 2 / g. Silicon nitride that is silicon and has an oxygen content of 0.4% or less.
なお、窒化ケイ素の粉砕性を評価するための上記粉砕機
としては、例えば化学工学便覧 昭和53年10月25日、丸
善株式会社の第1279〜1283頁に記載したものが使用され
る。すなわち、ジヨークラツシヤー、ジヤイレトリーク
ラツシヤー等の粗砕機、ロールクラツシヤー、ローラー
ミル、エツジランナー等の中砕機である。As the crusher for evaluating the pulverizability of silicon nitride, for example, the crusher described on pages 1279 to 1283 of Maruzen Co., Ltd., October 25, 1978, Chemical Engineering Handbook is used. That is, it is a coarse crusher such as a Dior crusher or a gyretory crusher, or a middle crusher such as a roll crusher, a roller mill or an edge runner.
以上のようにして得られた小さな粒状晶を有する本発明
のα−窒化ケイ素は、常法により、例えば、粗砕・中砕
後、ボールミル、振動ミル、ジエツトミル、アトライタ
ーミル、パールミル等で湿式・乾式粉砕し、α−窒化ケ
イ素粉末とする。粉末度については前述した少なくとも
平均粒子径を十分に留意し、粉砕機を含め、適切な条件
で処理する。The α-silicon nitride of the present invention having the small granular crystals obtained as described above is wet-processed by a conventional method, for example, after crushing / medium-crushing, using a ball mill, a vibration mill, a jet mill, an attritor mill, a pearl mill or the like.・ Dry pulverization to obtain α-silicon nitride powder. Regarding the fineness of powder, pay attention to at least the above-mentioned average particle diameter, and perform processing under appropriate conditions including a pulverizer.
次に、前記説明した窒化ケイ素粉末を用いた高温高強度
の窒化ケイ素質焼結体を得るに適した窒化ケイ素粉末組
成物について説明する。Next, a silicon nitride powder composition suitable for obtaining a high-temperature high-strength silicon nitride sintered body using the above-described silicon nitride powder will be described.
本発明の基本的技術思想は金属ケイ素直接窒化法で得ら
れた窒化ケイ素粉末であつて、しかも、低酸素である窒
化ケイ素原料を常圧焼結法を用いて、十分に焼結密度を
高めると共に、その焼結体を構成するβ−柱状晶のアス
ペクト比を大にせしめるに当つての、前記原料窒化ケイ
素粉末と焼結助剤の組合せの規制にある。The basic technical idea of the present invention is a silicon nitride powder obtained by the metal silicon direct nitriding method, and further, by using the atmospheric pressure sintering method of the silicon nitride raw material having low oxygen, the sintering density is sufficiently increased. At the same time, there is a regulation on the combination of the raw material silicon nitride powder and the sintering aid in increasing the aspect ratio of the β-columnar crystals constituting the sintered body.
窒化ケイ素粉末は種々の不純物を含んでおり、とりわけ
酸素が大半を占める。更に、説明するならば、この酸素
は添加される酸化物系焼結助剤と反応し粒界相を構成す
るので、その量は言うまでもなく、少ないことが好まし
い。つまり、高温高強度には低酸素は非常に重要であ
る。もちろん金属不純物は、前述したように高温クリー
プに影響を及ぼすので、少ない方が好ましい。Silicon nitride powder contains various impurities, most of which is oxygen. Further, to explain, this oxygen reacts with the oxide-based sintering aid to be added to form a grain boundary phase, and needless to say, its amount is preferably small. That is, low oxygen is very important for high temperature and high strength. Of course, the metal impurities affect the high temperature creep as described above, and therefore the smaller amount is preferable.
また、本発明で特筆すべきことは、低酸素が窒化ケイ素
のα→β転移における核発生に対し重要な役割をなして
いることである。つまり低酸素故に焼結助剤が構成する
液相への溶解度が低下し、不均質核生成が生じ、その結
果、異常とも思えるようなアスペクト比の高いβ柱状晶
を生成することがわかると共に、この効果の方が前述し
た粒界相の量低減化よりも高温高強度発現に対し有効で
あることを見出した。It is also noteworthy in the present invention that low oxygen plays an important role in nucleation in the α → β transition of silicon nitride. That is, because of the low oxygen, the solubility in the liquid phase of the sintering aid is lowered, heterogeneous nucleation occurs, and as a result, it is found that β columnar crystals with a high aspect ratio that may be considered abnormal are formed, It was found that this effect is more effective for high temperature and high strength development than the reduction of the amount of grain boundary phase described above.
更に、本発明者らは原料窒化ケイ素中の微粉末、例えば
特願昭63−277360号明細書に記載されているような0.2
μm下程度の微粉末が少なければ少ない程、恐らくこの
微粉末に多くの酸素が含まれていると考えられるが、前
述したα→β転移の不均質核発生に大きく寄与している
ことも見出した。Further, the present inventors have found that the fine powder in the raw material silicon nitride, for example 0.2% as described in Japanese Patent Application No. 63-277360.
It is considered that the smaller the amount of fine powder under μm is, the more oxygen is contained in this fine powder. However, it was also found that it contributes greatly to the heterogeneous nucleation of the α → β transition described above. It was
しかし、一般に原料窒化ケイ素粉末中の酸素が減少する
と通常の常圧焼結、例えばY2O3、Al2O3、SmO2、CeO2等
の1種又は2種以上の組合せた焼結助剤を7〜10%添加
しても、十分な焼結体密度が得られないのは周知の通り
である。However, in general, when oxygen in the raw material silicon nitride powder is reduced, normal pressureless sintering, for example, Y 2 O 3 , Al 2 O 3 , SmO 2 , CeO 2 or the like, or a combination of two or more sintering aids is used. It is well known that even if the agent is added in an amount of 7 to 10%, a sufficient sintered body density cannot be obtained.
以上説明したように、本発明の窒化ケイ素粉末は高温高
強度出現には最適な特性を備えている。しかし、低酸素
が故に常圧での焼結が非常に難しい。As described above, the silicon nitride powder of the present invention has optimum characteristics for the appearance of high temperature and high strength. However, it is very difficult to sinter under normal pressure because of low oxygen.
そこで、この難焼結機構が前述のハンプシヤらが述べて
いる相境界反応律速と考え、その律速を打破すると言わ
れている化合物を種々検討した結果、酸化マグネシウム
及び/又はその前駆物質を添加すれば、十分に焼結密度
が、常圧でも向上することを見出した。前駆物質として
は硝酸マグネシウム、炭酸マグネシウム、水酸化マグネ
シウム等であり、その添加量としては窒化ケイ素粉末組
成物として、5重量%未満で十分であることもわかつ
た。Therefore, this difficult sintering mechanism is considered to be the phase boundary reaction rate controlling described by Hampshire et al., And as a result of various studies on compounds that are said to break the rate controlling, magnesium oxide and / or its precursor is added. Then, it was found that the sintered density was sufficiently improved even at normal pressure. It was also found that the precursors were magnesium nitrate, magnesium carbonate, magnesium hydroxide and the like, and the addition amount of the silicon nitride powder composition was less than 5% by weight.
更に、前述したように粒界相の性状は高温強度発現には
重要であり、量はもちろんのこと分解温度がより高いこ
とが好ましいのは当然であり、そのためには希土類酸化
物と他の焼結助剤、例えば、Al2O3及び/又は窒化ケイ
素で構成される高融点粒界相を晶出せしめることも重要
なポイントである。希土類酸化物としてはY、La、Ce、
Pr、Nb、Sm、Eu等の酸化物が挙げられる。Further, as described above, the property of the grain boundary phase is important for high temperature strength development, and it is natural that it is preferable that the decomposition temperature is higher as well as the amount. It is also an important point to crystallize a high-melting-point grain boundary phase composed of a binder, for example, Al 2 O 3 and / or silicon nitride. As rare earth oxides, Y, La, Ce,
Oxides such as Pr, Nb, Sm and Eu can be mentioned.
以上のように、本発明の窒化ケイ素粉末と酸化マグネシ
ウム又はその前駆物質と希土類酸化物を含む焼結助剤か
らなる窒化ケイ素粉末組成物は、高温高強度発現には不
可欠である。なお、前記窒化ケイ素粉末組成物中の焼結
助剤は10重量%以内が好ましく、更に、焼結助剤中のMg
系化合物はMgO換算として、4重量%以内が適切であ
る。As described above, the silicon nitride powder composition of the present invention, which comprises the silicon nitride powder, magnesium oxide or the precursor thereof, and the sintering aid containing the rare earth oxide, is indispensable for achieving high temperature and high strength. Incidentally, the sintering aid in the silicon nitride powder composition is preferably within 10 wt%, further, Mg in the sintering aid
It is appropriate that the content of the compound is 4% by weight or less in terms of MgO.
また、更に言うならば、本発明の窒化ケイ素粉末は低酸
素であるから、前記説明した焼結助剤以外に独立的に液
相を作る系、又は若干低い温度領域で液相が生じる系の
焼結助剤を用いてもかまわない。In addition, to be more specific, since the silicon nitride powder of the present invention has low oxygen content, a system that independently forms a liquid phase other than the above-mentioned sintering aid, or a system that forms a liquid phase in a slightly low temperature range is used. A sintering aid may be used.
例えば、前者は酸化亜鉛、酸化ニツケル等を用いること
であり、後者は例えばY2O3−Al2O3でいえば、YAG組成程
度まで、Al2O3に富む組成にした焼結助剤を用いること
である。添加量についてはたとえば低酸素であつても、
焼結助剤量が多くなつてはガラス相が増加することにな
るので、12重量%以内が適切である。For example, the former is to use zinc oxide, nickel oxide, etc., and the latter is, for example, in the case of Y 2 O 3 -Al 2 O 3 , a sintering aid having a composition rich in Al 2 O 3 up to a YAG composition. Is to use. Regarding the amount of addition, for example, even if it is low oxygen,
If the amount of sintering aid is large, the glass phase will increase, so 12% by weight or less is appropriate.
次に、前記説明した窒化ケイ素粉末組成物の焼成した際
の窒化ケイ素質焼結体について説明する。Next, a silicon nitride-based sintered body obtained by firing the above-described silicon nitride powder composition will be described.
本発明の特徴はα→β転移で生成するアスペクト比の大
きいβ柱状晶が数多く見られることである。すなわちβ
柱状晶の大きさに関し不均質であるが、その不均質が例
えば数十μm単位の領域で均質である窒化ケイ素質焼結
体の組成であり、且つ、その組織が高温強度発現に重要
な役割をなしていることを見出したことにある。A feature of the present invention is that a large number of β columnar crystals having a large aspect ratio generated by α → β transition can be seen. Ie β
The composition of the silicon nitride sintered body is inhomogeneous with respect to the size of the columnar crystals, but the inhomogeneity is homogeneous in the region of, for example, several tens of μm, and its structure plays an important role in developing high temperature strength. It has been found to be doing.
一般に、高温強度発現は粒界相の強化、例えば高融点粒
界相を合成できるような焼結助剤の選択や、ガラス質の
結晶化等が主に研究されると共に、その研究の大半が焼
結側からのアプローチであつた。そこで、粉体側のアプ
ローチ、例えば、酸素の異なつた粉体、比表面積の異な
つた粉体、結晶化度の異なつた粉体等から焼結助剤一定
化下で種々実験した結果、単位密度当りの高温強度と焼
結体組織を構成するアスペクト比の高いβ柱状晶に大き
な相関があることを見出した。つまり、(30μm)×
(25μm)焼結体の視野中において、アスペクト比の大
きいと思われる5本のβ柱状晶の平均アスペクト比が10
以上あれば高温強度が単位密度当り250MPa以上発現する
ことを見出した。つまり、理論密度に近い値に焼結でき
れば十分に、1200℃の強度において、700MPa以上の発現
は十分に考えられるという感触を得た。この密度アツプ
阻害については前述してきた窒化ケイ素粉末中の酸素で
あり、微粉末である。また、この密度アツプ阻害の助長
が前述した窒化ケイ素粉末組成物中の酸化マグネシウム
である。In general, high temperature strength development is mainly researched on strengthening of the grain boundary phase, for example, selection of a sintering aid capable of synthesizing a high melting point grain boundary phase, crystallization of vitreous material, and most of the research. The approach was from the sintering side. Therefore, from the approach of the powder side, for example, powders with different oxygen, powders with different specific surface areas, powders with different crystallinity, etc. It was found that there is a strong correlation between the high temperature strength per hit and the β-columnar crystals with a high aspect ratio that make up the sintered structure. That is, (30 μm) ×
(25 μm) In the field of view of the sintered body, the average aspect ratio of the five β-columnar crystals that are considered to have a large aspect ratio is 10
It was found that the high-temperature strength exhibited 250 MPa or more per unit density if it was above. That is, it was felt that if the sintering could be performed to a value close to the theoretical density, the expression of 700 MPa or more could be sufficiently considered at the strength of 1200 ° C. The density up inhibition is oxygen in the silicon nitride powder described above and is a fine powder. Further, the promotion of the density up inhibition is magnesium oxide in the above-mentioned silicon nitride powder composition.
以上説明した本発明の窒化ケイ素質焼結体は十分に焼結
体密度が向上した組織であり且つ、不均質なβ柱状晶で
構成され且つ、その不均質なβ柱状晶の一部がアスペク
ト比の大きいものであり、更にそのミクロ的不均質組織
がマクロ的には均質になつている焼結体である。The above-described silicon nitride sintered body of the present invention has a structure in which the sintered body density is sufficiently improved, and is composed of inhomogeneous β columnar crystals, and a part of the inhomogeneous β columnar crystals has an aspect ratio. The sintered body has a large ratio, and its microscopic heterogeneous structure is macroscopically homogeneous.
本発明の窒化ケイ素質焼結体の製造方法については本発
明の窒化ケイ素粉末組成物を乾式又は湿式にて粉砕混合
し、次いで、所要の形状に成形後、不活性ガス下、例え
ば窒素、アルゴンガス下、1,600〜1,800℃の温度で、5
時間程度保持することにより、得られる。また、成形方
法の種類、例えばプレス成形、射出成形、スリツプキヤ
スト等、圧力、詰め粉等については特に限定はない。Regarding the method for producing the silicon nitride sintered body of the present invention, the silicon nitride powder composition of the present invention is pulverized and mixed by a dry method or a wet method, and then molded into a required shape, and then under an inert gas such as nitrogen or argon. 5 at a temperature of 1,600-1,800 ℃ under gas
It can be obtained by holding for about an hour. The type of molding method, such as press molding, injection molding, slip casting, pressure, filling powder, etc., is not particularly limited.
以上詳しく説明したように、本発明は窒化ケイ素粉末の
特性、具体的には酸素量、比表面積、平均粒子径、微粉
量及び金属不純物と高温強度との結びつきを検討し、特
に酸素量と微粉量が高温強度発現の相関を認め、更に、
前記特性となじみの深い焼結助剤を見出すと共にその焼
結体組織において非常にアスペクト比の高いβ柱状晶が
認められ、それが高温強度発現に重要な役割を果してい
ることを見出した。また、このような粉末をハロゲン化
ケイ素法ではなく、金属ケイ素粉末を特殊な雰囲気ガス
下で窒化し、次いで、常法により、粉砕して経済的に得
るものである。As described in detail above, the present invention examines the characteristics of silicon nitride powder, specifically, the amount of oxygen, the specific surface area, the average particle size, the amount of fine powder, and the relationship between the metal impurities and the high temperature strength, and particularly the amount of oxygen and the fine powder. The amount shows a correlation of high temperature strength development.
In addition to finding a sintering aid that is familiar with the above characteristics, β-columnar crystals with a very high aspect ratio were observed in the sintered body structure, and it was found that they play an important role in high temperature strength development. Further, such a powder is economically obtained by nitriding a metal silicon powder under a special atmosphere gas, and then pulverizing by a conventional method, not by a silicon halide method.
以下、実施例と比較例を挙げて更に具体的に本発明を説
明するが、本発明はこれら実施例に限定されない。Hereinafter, the present invention will be described more specifically with reference to Examples and Comparative Examples, but the present invention is not limited to these Examples.
なお、各例に示した測定値は次の方法によつた。The measured values shown in each example were obtained by the following method.
(1) 酸素(重量%): LECO社製 TC−136型O/N同時分析計による。(1) Oxygen (% by weight): By LECO TC-136 O / N simultaneous analyzer.
(2) 比表面積(m2/g): 湯浅アイオニクス社製のカンターソーブ Jr BET 1点法
による。(2) Specific surface area (m 2 / g): According to the Cantersorb Jr BET 1-point method manufactured by Yuasa Ionics.
(3) 粒子径(μm): 堀場製作所社製 CAPA−700による。(3) particle size ([mu] m): According to Horiba Ltd. C A P A -700.
(4) α分率(%): 理学電機社製のカイガーフラツクス RAD−II B型のX
線回折による。(4) α fraction (%): X of Kaiger Frax RAD-II B type manufactured by Rigaku Denki Co., Ltd.
By line diffraction.
(5) 金属不純物(ppm): JIS−G−1322に準拠した。(5) Metal impurities (ppm): Based on JIS-G-1322.
(Fe、Al、Ca) (6) 相対密度(%):アルキメデス法による。(Fe, Al, Ca) (6) Relative density (%): By Archimedes method.
(7) 3点曲げ強度(MPa): 島津製作所社製 オートグラフ AG−2000 A型による。(7) Three-point bending strength (MPa): According to Shimadzu Corporation Autograph AG-2000 A type.
実施例1〜7、比較例1〜4 金属Si純度99.98重量%の金属ケイ素粉末100重量部にα
分率90%で比表面積20m2/gの窒化ケイ素粉末10重量部混
合粉末2.5kgを第1表に示すカサ比重の150×150×20t程
度の窒化供試体に成形し、電気炉に充てんした。Examples 1 to 7, Comparative Examples 1 to 4 100 parts by weight of metallic silicon powder having a metallic Si purity of 99.98% by weight is α.
10 parts by weight of silicon nitride powder having a specific surface area of 20 m 2 / g with a fraction of 90% 2.5 kg of mixed powder was molded into a nitriding specimen having a bulk specific gravity of about 150 × 150 × 20 t shown in Table 1 and charged into an electric furnace. .
窒化に際しては第1表に示す通りに実施したがその際固
体のCaF2 2720gが充てんされ、且つ1,200℃に保持され
ている別の電気炉より、CaF2(G)(18〜36)/Hr(2
5℃)になるようにアルゴンガスで同伴させながら加熱
窒化した。Nitriding was performed as shown in Table 1, but at that time, from another electric furnace filled with 2720 g of solid CaF 2 and kept at 1,200 ° C, CaF 2 (G) (18 to 36) / Hr (2
It was heated and nitrided while being accompanied by argon gas so that the temperature became 5 ° C.
なお、比較例1〜4についてはCaF2(G)の導入なし
で、第1表に示す条件で加熱窒化した。In Comparative Examples 1 to 4, heating and nitriding were performed under the conditions shown in Table 1 without introducing CaF 2 (G).
得られた窒化ケイ素をSEM観察したところ、実施例1〜
9についてはすべて粒状化されていたが、比較例1〜4
はウイスカー、他形状の形態を呈していた。その1例と
して実施例1、比較例1、比較例3のSEM写真をそれぞ
れ第1図、第2図、第3図に示す。 SEM observation of the obtained silicon nitride revealed that
No. 9 was all granulated, but Comparative Examples 1 to 4
Had a whisker and other shapes. As one example, SEM photographs of Example 1, Comparative Example 1 and Comparative Example 3 are shown in FIGS. 1, 2 and 3, respectively.
得られた窒化ケイ素は粉砕・中砕(ジヨークラツシヤー
及びトツプグラインダー)で0.2mm下に粉砕し、更に、
内容積1のボールミルに0.2mm下の粉砕品50g、4φFe
ボール0.5、水100gを入れ、20Hr湿式粉砕後、塩酸と
フツ酸で酸処理し、過・乾燥・解砕を行い、焼結原料
用窒化ケイ素粉末を製造した。得られた窒化ケイ素粉末
について、酸素、平均粒子径、比表面積、0.2μm以
下、Fe+Al+Caの含有量の測定を行い、第2表に示し
た。The obtained silicon nitride is crushed and crushed (Jiyo crusher and top grinder) to crush 0.2 mm below.
50 mm of crushed products under 0.2 mm in a ball mill with an internal volume of 1 and 4φ Fe
A ball 0.5 and 100 g of water were put in, wet pulverized for 20 hours, then acid-treated with hydrochloric acid and hydrofluoric acid, over-dried and crushed to produce silicon nitride powder as a sintering raw material. The obtained silicon nitride powder was measured for oxygen, average particle size, specific surface area, 0.2 μm or less, and Fe + Al + Ca content, and the results are shown in Table 2.
次に、この窒化ケイ素粉末の内割で平均粒子径1.3μm
のY2O3と平均粒子径1.4μmのAl2O3、平均粒子径1.2μ
mのMgOをそれぞれ5重量%、2重量%、3重量%添加
し、更に、1,1,1−トリクロロエタンを加えて4時間ボ
ールミルで湿式混合し、乾燥後、100kg/cm2の成形圧で
6×10×60mm形状に金型成形した後、2700kg/cm2の成形
圧でCIP成形した。これらの成形体をカーボンルツボに
セツトし、N2ガス雰囲気中、第2表に示す条件で焼成し
て焼結体を得た。得られた焼結体は研削後、相対密度と
常温、高温の3点曲げ強度を測定した。それらの結果を
第2表に示す。Next, the average particle size of this silicon nitride powder is 1.3 μm
Y 2 O 3 and average particle size 1.4 μm Al 2 O 3 , average particle size 1.2 μm
5% by weight, 2% by weight and 3% by weight of MgO are added, respectively, 1,1,1-trichloroethane is further added, and the mixture is wet mixed in a ball mill for 4 hours, dried, and then molded at a molding pressure of 100 kg / cm 2. After molding into a 6 × 10 × 60 mm shape, CIP molding was performed at a molding pressure of 2700 kg / cm 2 . These compacts were set in a carbon crucible and fired under N 2 gas atmosphere under the conditions shown in Table 2 to obtain sintered compacts. After the obtained sintered body was ground, the relative density and the three-point bending strength at normal temperature and high temperature were measured. The results are shown in Table 2.
実施例8〜9 金属不純物としてのFe、Al及びCaの影響を知るために、
実施例1の窒化ケイ素粉末を焼結する際に、あらかじめ
準備されたFe−Al−Caの合金粉末を第3表に示すように
添加し、実施例1と同様な条件で焼結体を製造した。得
られた焼結体特性を第3表に示す。 Examples 8-9 In order to know the effect of Fe, Al and Ca as metal impurities,
When the silicon nitride powder of Example 1 was sintered, Fe-Al-Ca alloy powder prepared in advance was added as shown in Table 3, and a sintered body was manufactured under the same conditions as in Example 1. did. The properties of the obtained sintered body are shown in Table 3.
実施例10〜11 この実施例は、窒化ケイ素の粉末度の影響を知るために
行つたものである。実施例1で得られた窒化ケイ素を湿
式粉砕するに際し、湿式粉砕時間を2Hr(実施例10)、4
0Hr(実施例11)に変えた以外は実施例1と同様に窒化
ケイ素粉末を得、焼結体を製造した。その結果を第4表
に示す。 Examples 10 to 11 This example was conducted to find out the effect of the fineness of silicon nitride. When wet-milling the silicon nitride obtained in Example 1, the wet-milling time was set to 2 Hr (Example 10), 4
A silicon nitride powder was obtained in the same manner as in Example 1 except that 0Hr (Example 11) was used to produce a sintered body. The results are shown in Table 4.
実施例12〜17、比較例5 この実施例ではハロゲンガスの種類を変えて行つた。 Examples 12 to 17 and Comparative Example 5 In this example, the kind of halogen gas was changed.
実施例1と同様な原料、窒化供試体及び充てん量で、第
5表に示す窒化条件を用い加熱窒化した。ハロゲンガス
の導入方法については実施例1と同様に行つた。なお、
実施例12についてはハロゲンガスの導入温度を1,150℃
〜1,350℃とした。また、実施例17についてはハロゲン
ガスの導入方法を別の炉からではなく、同一炉内の窒化
供試体の傍に固体のCaF2を成形し置き、昇華させながら
窒化を行つた。比較例5についてはハロゲンガスの導入
は行わなかつた。The same raw material, nitriding sample, and filling amount as in Example 1 were used and the heat nitriding was performed under the nitriding conditions shown in Table 5. The method of introducing the halogen gas was the same as in Example 1. In addition,
For Example 12, the introduction temperature of the halogen gas was 1,150 ° C.
It was set to ~ 1,350 ° C. In addition, in Example 17, solid CaF 2 was molded and placed beside the nitriding specimen in the same furnace as the method of introducing the halogen gas, not from another furnace, and nitriding was performed while sublimating. Regarding Comparative Example 5, introduction of halogen gas was not performed.
得られた窒化ケイ素は実施例1と同様な方法で湿式粉砕
し、窒化ケイ素粉末を得た。得られた粉体特性を第5表
に示す。The obtained silicon nitride was wet-ground in the same manner as in Example 1 to obtain a silicon nitride powder. The powder characteristics obtained are shown in Table 5.
得られた窒化ケイ素粉末は実施例1と同様な方法で焼結
を行い、焼結体を製造し、評価した。その結果を第5表
に示す。The obtained silicon nitride powder was sintered in the same manner as in Example 1 to manufacture and evaluate a sintered body. The results are shown in Table 5.
本発明のようにアスペクト比の高いβ柱状晶(実施例
1)並びに比較例のアスペクト比の低いβ柱状晶(比較
例5)の粒子構造の組織図をそれぞれ第4図、第5図に
示す。The grain structure diagrams of the β columnar crystals having a high aspect ratio (Example 1) as in the present invention and the β columnar crystals having a low aspect ratio of the comparative example (Comparative Example 5) are shown in FIGS. 4 and 5, respectively. .
なお、第4図及び第5図は倍率7500倍のSEM写真であ
る。4 and 5 are SEM photographs with a magnification of 7500 times.
第4図はアスペクト比10以上のβ柱状晶が多数見られる
不均質の均質組織からなつているのに対し、第5図は比
較的アスペクト比の低い(≒5程度)均質組成からなつ
ていることがわかる。Fig. 4 consists of an inhomogeneous homogeneous structure with many β-columnar crystals with an aspect ratio of 10 or more, while Fig. 5 consists of a homogeneous composition with a relatively low aspect ratio (approximately 5). I understand.
実施例18〜26、比較例6及び7 この実施例は、焼結助剤の種類と量を変えたものであ
る。実施例18〜26は、実施例1において、焼結助剤を第
6表に変えたこと以外は、同様にして焼結体を製造した
ものである。 Examples 18-26, Comparative Examples 6 and 7 In this example, the type and amount of the sintering aid was changed. In Examples 18 to 26, sintered bodies were produced in the same manner as in Example 1 except that the sintering aid was changed to that shown in Table 6.
比較例6及び7は、実施例25と26において、使用した窒
化ケイ素粉末を、比較例5のものに代えて用いたもので
ある。それらの結果を第6表に示す。In Comparative Examples 6 and 7, the silicon nitride powder used in Examples 25 and 26 was used instead of that in Comparative Example 5. The results are shown in Table 6.
実施例27〜33、比較例8及び9 この実施例は、焼結条件を変えたものである。実施例1
の窒化ケイ素粉末組成物を用い、第7表に示す条件で、
焼結を行つたこと以外は、実施例1と同様にして焼結体
を製造した。比較例8と9は実施例1の窒化ケイ素粉末
の代りに、比較例5の粉末を用いたものである。それら
の結果を第7表に示す。 Examples 27-33, Comparative Examples 8 and 9 In this example, the sintering conditions were changed. Example 1
Using the silicon nitride powder composition of, under the conditions shown in Table 7,
A sintered body was manufactured in the same manner as in Example 1 except that sintering was performed. In Comparative Examples 8 and 9, the powder of Comparative Example 5 was used instead of the silicon nitride powder of Example 1. The results are shown in Table 7.
〔発明の効果〕 本発明により製造された窒化ケイ素粉末は低酸素で、Mg
O−Al2O3−Y2O3系の焼結助剤を用いて常圧焼結した場
合、1200℃の高温曲げ強度が700MPa以上の粉末である。 [Effect of the invention] The silicon nitride powder produced by the present invention is low oxygen, Mg
When pressure-sintered with an O—Al 2 O 3 —Y 2 O 3 -based sintering aid, the powder has a high-temperature bending strength at 1200 ° C. of 700 MPa or more.
これは焼結体のβ−柱状晶の発生とその成長に関係する
粉体特性を制御した結果によるものである。This is a result of controlling the powder properties related to the generation and growth of β-columnar crystals in the sintered body.
第1図、第2図、第3図は実施例1、比較例1、3で得
られた窒化ケイ素の粒子構造の形態を示す倍率3,500倍
のSEM写真、第4図、第5図は実施例1、比較例5で得
られた窒化ケイ素焼結体の粒子構造の組織図を示す倍率
7,500倍のSEM写真である。FIGS. 1, 2, and 3 are SEM photographs at a magnification of 3,500 showing the morphology of the silicon nitride particle structures obtained in Example 1 and Comparative Examples 1 and 3, and FIGS. Magnification showing a structural diagram of the grain structure of the silicon nitride sintered bodies obtained in Example 1 and Comparative Example 5.
It is a SEM photograph of 7,500 times.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C04B 35/626 (72)発明者 広津留 秀樹 福岡県大牟田市新開町1 電気化学工業株 式会社大牟田工場内 (56)参考文献 特開 昭54−22000(JP,A) 特開 昭64−37469(JP,A)─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI Technical display location C04B 35/626 (72) Inventor Hideki Hirotsuru 1 Shinkaimachi, Omuta City, Fukuoka Prefecture Electrochemical Industry Co., Ltd. Omuta Plant (56) References JP 54-22000 (JP, A) JP 64-37469 (JP, A)
Claims (1)
で金属ケイ素粉末を窒化して窒化ケイ素を製造する方法
において、アルカリ金属ハロゲン化物及びアルカリ土類
金属ハロゲン化物よりなる群から選択したハロゲン化物
の少なくとも1種を、気体の状態で連続的、間欠的又は
一時的に供給することを特徴とする窒化ケイ素の製造方
法。1. A method for producing silicon nitride by nitriding a metal silicon powder in an atmosphere containing nitrogen and / or ammonia, comprising a halide selected from the group consisting of alkali metal halides and alkaline earth metal halides. A method for producing silicon nitride, which comprises continuously, intermittently, or temporarily supplying at least one kind in a gas state.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1043079A JPH07102966B2 (en) | 1989-02-27 | 1989-02-27 | Method for manufacturing silicon nitride |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1043079A JPH07102966B2 (en) | 1989-02-27 | 1989-02-27 | Method for manufacturing silicon nitride |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH02225304A JPH02225304A (en) | 1990-09-07 |
| JPH07102966B2 true JPH07102966B2 (en) | 1995-11-08 |
Family
ID=12653837
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1043079A Expired - Fee Related JPH07102966B2 (en) | 1989-02-27 | 1989-02-27 | Method for manufacturing silicon nitride |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH07102966B2 (en) |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE102012207803A1 (en) * | 2012-05-10 | 2013-11-28 | Schaeffler Technologies AG & Co. KG | Silicon nitride ceramics and process for their preparation |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6047203B2 (en) * | 1977-07-19 | 1985-10-21 | 電気化学工業株式会社 | Method for manufacturing α-type silicon nitride |
| JP2526598B2 (en) * | 1987-08-04 | 1996-08-21 | 株式会社長野計器製作所 | Method for manufacturing silicon nitride ceramics |
-
1989
- 1989-02-27 JP JP1043079A patent/JPH07102966B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH02225304A (en) | 1990-09-07 |
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