JPH0948670A - Silicon nitride powder and its production - Google Patents
Silicon nitride powder and its productionInfo
- Publication number
- JPH0948670A JPH0948670A JP7214173A JP21417395A JPH0948670A JP H0948670 A JPH0948670 A JP H0948670A JP 7214173 A JP7214173 A JP 7214173A JP 21417395 A JP21417395 A JP 21417395A JP H0948670 A JPH0948670 A JP H0948670A
- Authority
- JP
- Japan
- Prior art keywords
- silicon
- powder
- silicon nitride
- aluminum oxide
- reaction
- 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.)
- Pending
Links
- 239000000843 powder Substances 0.000 title claims abstract description 53
- 229910052581 Si3N4 Inorganic materials 0.000 title claims abstract description 40
- HQVNEWCFYHHQES-UHFFFAOYSA-N silicon nitride Chemical compound N12[Si]34N5[Si]62N3[Si]51N64 HQVNEWCFYHHQES-UHFFFAOYSA-N 0.000 title claims abstract description 40
- 238000004519 manufacturing process Methods 0.000 title claims description 5
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 claims abstract description 67
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 claims abstract description 36
- 238000005121 nitriding Methods 0.000 claims abstract description 34
- 238000006243 chemical reaction Methods 0.000 claims abstract description 28
- 239000011863 silicon-based powder Substances 0.000 claims abstract description 24
- 239000012535 impurity Substances 0.000 claims abstract description 21
- 239000001301 oxygen Substances 0.000 claims abstract description 19
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 19
- 239000012298 atmosphere Substances 0.000 claims abstract description 18
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 18
- 229910052751 metal Inorganic materials 0.000 claims description 26
- 239000002184 metal Substances 0.000 claims description 26
- 238000010438 heat treatment Methods 0.000 abstract description 28
- 229910052710 silicon Inorganic materials 0.000 description 43
- 239000010703 silicon Substances 0.000 description 43
- LIVNPJMFVYWSIS-UHFFFAOYSA-N silicon monoxide Chemical compound [Si-]#[O+] LIVNPJMFVYWSIS-UHFFFAOYSA-N 0.000 description 30
- 239000007789 gas Substances 0.000 description 19
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 18
- 239000000463 material Substances 0.000 description 17
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 12
- 239000002245 particle Substances 0.000 description 10
- 229910052814 silicon oxide Inorganic materials 0.000 description 10
- 239000007795 chemical reaction product Substances 0.000 description 9
- 238000000034 method Methods 0.000 description 8
- 238000001816 cooling Methods 0.000 description 7
- 229910004298 SiO 2 Inorganic materials 0.000 description 6
- 150000001875 compounds Chemical class 0.000 description 6
- 229910001873 dinitrogen Inorganic materials 0.000 description 6
- 229910052757 nitrogen Inorganic materials 0.000 description 6
- 230000000694 effects Effects 0.000 description 4
- 238000009434 installation Methods 0.000 description 4
- 150000004767 nitrides Chemical class 0.000 description 4
- 238000000634 powder X-ray diffraction Methods 0.000 description 4
- 230000000007 visual effect Effects 0.000 description 4
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- 239000002244 precipitate Substances 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 230000000630 rising effect Effects 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- 229910002795 Si–Al–O–N Chemical class 0.000 description 2
- 229910052786 argon Inorganic materials 0.000 description 2
- 229910052791 calcium Inorganic materials 0.000 description 2
- 239000011575 calcium Substances 0.000 description 2
- 239000013078 crystal Substances 0.000 description 2
- 229910052734 helium Inorganic materials 0.000 description 2
- 239000010410 layer Substances 0.000 description 2
- 239000012299 nitrogen atmosphere Substances 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 238000007670 refining Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 238000003786 synthesis reaction Methods 0.000 description 2
- 230000002194 synthesizing effect Effects 0.000 description 2
- 229910018516 Al—O Inorganic materials 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- 238000002441 X-ray diffraction Methods 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 235000012255 calcium oxide Nutrition 0.000 description 1
- 239000000306 component Substances 0.000 description 1
- PMHQVHHXPFUNSP-UHFFFAOYSA-M copper(1+);methylsulfanylmethane;bromide Chemical compound Br[Cu].CSC PMHQVHHXPFUNSP-UHFFFAOYSA-M 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000003795 desorption Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005755 formation reaction Methods 0.000 description 1
- 239000001307 helium Substances 0.000 description 1
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 1
- 229910001337 iron nitride Inorganic materials 0.000 description 1
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N iron oxide Inorganic materials [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 1
- 235000013980 iron oxide Nutrition 0.000 description 1
- VBMVTYDPPZVILR-UHFFFAOYSA-N iron(2+);oxygen(2-) Chemical class [O-2].[Fe+2] VBMVTYDPPZVILR-UHFFFAOYSA-N 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 150000002926 oxygen Chemical class 0.000 description 1
- 238000004451 qualitative analysis Methods 0.000 description 1
- 238000004445 quantitative analysis Methods 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 239000006104 solid solution Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000002344 surface layer Substances 0.000 description 1
- 229910021654 trace metal Inorganic materials 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
Landscapes
- Ceramic Products (AREA)
- Solid-Phase Diffusion Into Metallic Material Surfaces (AREA)
Abstract
Description
【0001】[0001]
【発明が属する技術分野】この発明は高純度α型窒化珪
素粉末、及びその製造方法に関する。TECHNICAL FIELD The present invention relates to a high-purity α-type silicon nitride powder and a method for producing the same.
【0002】[0002]
【従来技術】金属珪素粉末を窒素源となる物質、例えば
窒素ガス等と反応させて直接窒化させることによりα型
窒化珪素粉末の合成が行われている。この方法は合成プ
ロセスが比較的単純である為、工業的規模での量産化に
適している。2. Description of the Related Art α-type silicon nitride powder is synthesized by reacting metallic silicon powder with a substance serving as a nitrogen source, for example, nitrogen gas and directly nitriding it. This method is suitable for mass production on an industrial scale because the synthesis process is relatively simple.
【0003】この金属珪素粉末は、珪素源である珪石精
製上の制約から、一般に不可避不純物として微量の酸素
が含まれている他、その表面は極めて容易に酸化され易
く、通常は表層部に酸化珪素が形成されたものとなって
いる為、実際に使用する珪素粉末の殆どは数重量%程度
の酸素が含まれている。[0003] This metallic silicon powder generally contains a trace amount of oxygen as an unavoidable impurity due to restrictions in refining silica, which is a silicon source, and the surface thereof is extremely easily oxidized and is usually oxidized on the surface layer portion. Since silicon is formed, most of the silicon powders actually used contain about several wt% of oxygen.
【0004】金属珪素を直接窒化することにより高純度
の窒化珪素粉末を得るには、この酸素を除去する必要が
ある。しかし酸素のみを選択的に除去するのは困難であ
り、通常は一酸化珪素、又は珪素以外に不純物として含
まれる微量金属との酸化物の形で高温気化することで除
去されている。In order to obtain high-purity silicon nitride powder by directly nitriding metallic silicon, it is necessary to remove this oxygen. However, it is difficult to selectively remove only oxygen, and it is usually removed by high-temperature vaporization in the form of silicon monoxide or an oxide with a trace metal contained as impurities other than silicon.
【0005】このように表面酸素を除去した金属珪素を
直接窒化によってα型窒化珪素を合成する反応は、発熱
反応となるが、金属珪素の融点は1410℃前後である
ことから、過度の反応が起こると金属珪素が溶融し、そ
の比表面積が極度に減少することから合成反応が進行し
難くなる。The reaction of synthesizing α-type silicon nitride by directly nitriding metallic silicon from which surface oxygen has been removed in this way is an exothermic reaction, but since the melting point of metallic silicon is around 1410 ° C., an excessive reaction occurs. When this occurs, the metallic silicon is melted and its specific surface area is extremely reduced, so that the synthesis reaction is difficult to proceed.
【0006】この為α型窒化珪素を安定して合成する為
に、種々の方策が検討実施されてきた。即ち、低温領域
で長時間反応させること、又は窒化の反応熱で原料温度
が急上昇しないように雰囲気の窒素分圧を下げて反応温
度の上昇を抑え、窒化反応熱で原料温度が急上昇しない
ようにする等の方策の他、雰囲気中にAr、Heや金属
珪素の表面酸素を還元する効果もあるH2、NH3、等の
ガスを混合することで、雰囲気ガスの熱伝導度を上げ反
応原料が蓄熱されるのを防ぐことも行われている。更
に、高純度の窒化珪素を必要としない場合は、金属珪素
にカルシウム、鉄等の酸化物、窒化物を添加することに
より、窒化反応を促進させると共にα型窒化珪素を高い
生産性で安定して合成することも行われている。Therefore, various measures have been studied and implemented in order to stably synthesize α-type silicon nitride. That is, the reaction is performed for a long time in a low temperature region, or the reaction temperature is suppressed from rising by lowering the nitrogen partial pressure of the atmosphere so that the reaction temperature of nitriding does not cause a sudden increase in the raw material temperature, and the nitriding reaction heat prevents the raw material temperature from rapidly increasing. In addition to the above measures, by mixing gases such as H 2 , NH 3 and the like, which also have the effect of reducing surface oxygen of Ar, He and metallic silicon in the atmosphere, the thermal conductivity of the atmosphere gas is increased. It is also done to prevent the heat from being stored. Further, when high-purity silicon nitride is not required, the addition of calcium or iron oxides or nitrides to metallic silicon promotes the nitriding reaction and stabilizes α-type silicon nitride with high productivity. It is also done by synthesizing.
【0007】[0007]
【発明が解決しようとする課題】金属珪素表面に珪素酸
化物が形成されていると、直接窒化を行う際に、表面の
酸化物層によって窒化性ガスと金属珪素との直接接触・
反応が阻害され、窒化反応が低下し、未窒化の珪素が存
在したり、多大な反応時間を要すことがあった。更に、
高温時に金属珪素表面の珪素酸化物が分解しSiOガス
として気化する為、この発生したSiOガスが加熱装置
内のヒーター材と反応してヒーターを腐食する他、加熱
装置の冷却部、或いは低温部分の部材上に析出する傾向
があるので装置の冷却効果が落ちたり、装置寿命の短縮
化に繋がることがあった。また、SiOガスは生成した
窒化珪素と反応して窒化珪素表面に酸窒化珪素化合物を
生成することもある。このように表面に多くの酸素が含
まれる金属珪素を直接窒化した窒化珪素粉末は、酸窒化
物を生成したり、未反応の金属珪素が残り、高純度、か
つ高いα化率の窒化珪素が得られなかった。When silicon oxide is formed on the surface of metallic silicon, when the direct nitriding is carried out, the nitriding gas and metallic silicon are directly contacted by the oxide layer on the surface.
In some cases, the reaction was hindered, the nitriding reaction decreased, unnitrided silicon was present, and a long reaction time was required. Furthermore,
At high temperature, the silicon oxide on the surface of metallic silicon decomposes and vaporizes as SiO gas, and the generated SiO gas reacts with the heater material in the heating device to corrode the heater, and also the cooling part of the heating device or the low temperature part. Since it tends to be deposited on the member, the cooling effect of the device may be reduced or the life of the device may be shortened. Further, the SiO gas may react with the produced silicon nitride to produce a silicon oxynitride compound on the surface of the silicon nitride. In this way, the silicon nitride powder obtained by directly nitriding metallic silicon containing a large amount of oxygen on the surface thereof produces oxynitride or remains unreacted metallic silicon, resulting in high-purity and high-alpha silicon nitride. I couldn't get it.
【0008】[0008]
【課題を解決するための手段】本発明者らは前記課題解
決の為、窒化性雰囲気中に於いて、酸化アルミニウム粉
末共存下で金属珪素を加熱すると、金属珪素表面に形成
されている酸化珪素の気化したSiOが、ヒーターを含
む加熱炉材に殆ど影響を及ぼすことなく、選択的に酸化
アルミニウム粉末に速やかに捕捉され、少なくともその
表面に酸素が存在しない珪素が窒化反応に用いられて、
高純度の窒化珪素を得ることができ、しかもこの窒化は
1200℃程度の比較的低い温度から始まる為、α型窒
化珪素になり易いことを見出し、本発明を完成させた。In order to solve the above problems, the present inventors have found that when metallic silicon is heated in the presence of aluminum oxide powder in a nitriding atmosphere, the silicon oxide formed on the surface of the metallic silicon. The vaporized SiO 2 is selectively captured rapidly by the aluminum oxide powder with little effect on the heating furnace material including the heater, and at least silicon having no oxygen on its surface is used for the nitriding reaction,
The inventors have found that high-purity silicon nitride can be obtained, and that this nitriding starts from a relatively low temperature of about 1200 ° C., so that α-type silicon nitride is likely to be formed, and the present invention has been completed.
【0009】即ち、この発明は酸素を含む金属珪素粉末
を、該粉末と接触させずに共存させた酸化アルミニウム
粉末と共に、窒化性雰囲気中で加熱して成るα化率が9
6%以上で金属不純物が0.4重量%以下であることを
特徴とする窒化珪素粉末である。That is, according to the present invention, a metal silicon powder containing oxygen is heated in an nitriding atmosphere together with an aluminum oxide powder coexisting without being brought into contact with the powder, and the α-conversion rate is 9.
The silicon nitride powder is characterized by containing 6% or more and 0.4% by weight or less of metal impurities.
【0010】またこの発明は、酸素を含む金属珪素粉末
を、該粉末と接触させずに共存させた酸化アルミニウム
粉末と共に、窒化性雰囲気中で加熱して成るα化率が9
6%以上で金属不純物が0.4重量%以下であることを
特徴とする窒化珪素粉末の製造方法である。Further, according to the present invention, the α-conversion rate obtained by heating metallic silicon powder containing oxygen together with aluminum oxide powder coexisting without contacting the powder in a nitriding atmosphere is 9
The method for producing a silicon nitride powder is characterized in that 6% or more and 0.4% by weight or less of metal impurities.
【0011】通常市販されている金属珪素粉末は極めて
酸化され易く、一般には表面部を中心に、主として非晶
質構造の酸化珪素が生成しており、一旦この酸化珪素層
が表面に形成されるとそれ以上殆ど酸化されず安定にな
る。本発明に於いて対象とする金属珪素とはこのような
状態のものであり、概ね3重量%以下の酸素をその表面
部を中心に含んでいるものである。The commercially available metallic silicon powder is extremely susceptible to oxidation, and generally, silicon oxide having an amorphous structure is mainly formed mainly on the surface portion, and this silicon oxide layer is once formed on the surface. And it becomes stable with almost no oxidation. The metallic silicon that is the object of the present invention is in such a state, and contains approximately 3% by weight or less of oxygen mainly in its surface portion.
【0012】また、この発明の窒化珪素粉末は96%以
上がα型の結晶からなり、またその純度は、金属珪素精
製段階から不可避的に含まれる例えばFe、Al、Ca
等の金属と金属珪素からなる不純物が0.4重量%以下
である。Further, the silicon nitride powder of the present invention comprises 96% or more of α-type crystals, and its purity is, for example, Fe, Al, Ca which is inevitably contained in the metallic silicon refining stage.
Impurities made of metal such as metal and silicon are 0.4 wt% or less.
【0013】このような窒化珪素粉末は以下のような方
法によって製造される。即ち、原料としては、前記のよ
うな表面部を主に概ね0.5〜3重量%の酸素を含んだ
金属珪素粉末を用いる。その粒径としてはより小さいも
の、例えば105μm以下のものが望ましい。粒径が大
きい金属珪素では窒化反応に時間がかかり、また完全に
内部まで窒化しないこともあるので好ましくない。この
酸素を含んだ金属珪素粉末を大気と隔絶可能な加熱室を
有する加熱炉に設置する。加熱炉は大気と隔絶可能な加
熱室を有し、かつ加熱室に窒素等の雰囲気ガスを供給で
きるものであれば何れのものでも良いが、例えば雰囲気
制御可能なバッチ炉、プッシャー炉、トンネル炉、ベル
ト炉等を用いることが出来る。Such a silicon nitride powder is manufactured by the following method. That is, as the raw material, metallic silicon powder containing oxygen in an amount of approximately 0.5 to 3% by weight on the surface as described above is used. The particle size is preferably smaller, for example, 105 μm or less. Metallic silicon having a large particle size is not preferable because the nitriding reaction takes a long time and the inside may not be completely nitrided. This metallic silicon powder containing oxygen is placed in a heating furnace having a heating chamber capable of being isolated from the atmosphere. The heating furnace may be any one as long as it has a heating chamber that can be isolated from the atmosphere and can supply an atmosphere gas such as nitrogen to the heating chamber. For example, a batch furnace, a pusher furnace, a tunnel furnace that can control the atmosphere. A belt furnace or the like can be used.
【0014】加熱炉への金属珪素粉末と共存させる酸化
アルミニウム粉末の設置方法としては、金属珪素粉末
を、例えば反応焼結窒化珪素等の材質からなる容器に入
れ、これを加熱炉に設置する。酸化アルミニウム粉末は
直接炉床に敷いても良く、また炉床材及び酸化アルミニ
ウムの何れとも反応しない材質からなる開口容器中に収
納したものを設置するのが良い。加熱炉内での酸化アル
ミニウム粉末と金属珪素粉末の設置位置は互いに接触さ
せずにできるだけ近い位置に設置するのが良く、例えば
バッチ炉であれば最下段の棚板に酸化アルミニウム粉末
を積載し、その上段の棚板上に金属珪素粉末を積載す
る。或いは、連続炉であれば同一の棚板上に酸化アルミ
ニウム粉末を入れた通気孔を有する別の収納容器を設置
してもよい。共存させる酸化アルミニウム粉末はその絶
対量よりも、炉内で酸化アルミニウム粉末が占める存在
面積が大であるほど一度に捕捉できる酸化珪素捕捉容量
が増大するので好ましい。通常は処理する金属珪素重量
の10%程度の量を用いれば十分である。As a method of installing the aluminum oxide powder to be coexistent with the metallic silicon powder in the heating furnace, the metallic silicon powder is placed in a container made of a material such as reaction-sintered silicon nitride and placed in the heating furnace. The aluminum oxide powder may be laid directly on the hearth, or may be placed in an open container made of a material that does not react with any of the hearth material and aluminum oxide. The aluminum oxide powder and the metal silicon powder in the heating furnace are preferably installed at positions as close to each other as possible without contacting each other.For example, in the case of a batch furnace, the aluminum oxide powder is loaded on the bottom shelf plate, Metallic silicon powder is loaded on the upper shelf. Alternatively, in the case of a continuous furnace, another storage container having a vent hole containing aluminum oxide powder may be installed on the same shelf plate. It is preferable that the coexisting aluminum oxide powder has a larger area occupied by the aluminum oxide powder in the furnace than the absolute amount thereof, because the silicon oxide trapping capacity that can be trapped at one time increases. It is usually sufficient to use an amount of about 10% of the weight of metallic silicon to be treated.
【0015】本発明で用いる酸化アルミニウム粉末は、
α型、γ型何れの結晶でもよいが、高活性なγ型の方が
より好ましい。また酸化アルミニウムに含まれる不純物
としては、金属珪素の窒化や金属珪素からの珪素酸化物
の離脱やその吸収、更に生成した窒化珪素の純度等に影
響を及ぼさない不純物である限り含まれても良い。この
ような許容可能な不純物は、いわゆる市販廉価品に於い
て通常含まれているようなものでも良く、またそれらの
概ね許容出来得る含有量としては約5%程度である。こ
のような酸化アルミニウムの粒径は小さい方が大きい表
面積を有するが故により表面エネルギーが高く、気化し
た酸化珪素を捕え易くなるので好ましい。また、本発明
で用いる酸化アルミニウム粉末は、好ましくは単粒子化
されているものが良いが、凝集粒や粉末圧粉体であって
も用いることが出来る。The aluminum oxide powder used in the present invention is
Both α-type and γ-type crystals may be used, but the highly active γ-type is more preferable. Further, the impurities contained in aluminum oxide may be contained as long as they do not affect the nitriding of metal silicon, the removal and absorption of silicon oxide from metal silicon, and the purity of generated silicon nitride. . Such acceptable impurities may be those which are usually contained in so-called low-priced commercial products, and their content is about 5%. The smaller the particle size of such aluminum oxide is, the larger the surface area is because the aluminum oxide has a large surface area, and the vaporized silicon oxide is easily trapped, which is preferable. The aluminum oxide powder used in the present invention is preferably in the form of single particles, but aggregated particles or powder compacts can also be used.
【0016】金属珪素粉末の直接窒化による窒化物生成
反応に必要な温度は、1200℃以下の温度では窒化反
応が起こらないか極めて緩慢な反応となる為、少なくと
も1200℃を越える温度であれば優れた窒化効率で窒
化物を生成することができるが、より高い窒化率で安定
して得るには1410℃以上が好ましい。また1500
℃を越える温度ではβ型窒化珪素が合成され易くなる為
好ましくない。また、本発明における窒化性雰囲気と
は、珪素金属を所定の温度で直接窒化し、窒化物を生成
させることが可能な雰囲気であれば良く、窒素を主体と
してアルゴン、ヘリウム、水素、アンモニア等が少量混
合した混合ガスを用いても良いが、炉材やヒーター材の
腐食を抑える観点から、さらには比較的安価であるとい
う点からも窒素ガス単独が最も良い。本発明の窒化珪素
粉末は前記のような設置・加熱条件下で金属珪素を直接
窒化させた後、反応生成物を炉内で常温近傍まで自然放
冷等冷却することにより製造することができる。The temperature required for the nitride formation reaction by direct nitriding of metal silicon powder is 1200 ° C. or lower, and the nitriding reaction does not occur or is extremely slow. Therefore, a temperature exceeding 1200 ° C. is excellent. Although it is possible to generate a nitride with a high nitriding efficiency, 1410 ° C. or higher is preferable in order to stably obtain a higher nitriding rate. Again 1500
If the temperature exceeds ℃, β-type silicon nitride is easily synthesized, which is not preferable. Further, the nitriding atmosphere in the present invention may be an atmosphere in which silicon metal can be directly nitrided at a predetermined temperature to generate a nitride, and nitrogen is the main component, and argon, helium, hydrogen, ammonia, etc. A mixed gas mixed in a small amount may be used, but nitrogen gas alone is the best from the viewpoint of suppressing the corrosion of the furnace material and heater material, and also from the viewpoint of being relatively inexpensive. The silicon nitride powder of the present invention can be produced by directly nitriding metallic silicon under the above-mentioned installation and heating conditions, and then naturally cooling the reaction product to near room temperature in the furnace.
【0017】[0017]
【作用及び発明の効果】この発明に於ける酸化アルミニ
ウムは以下のような作用により金属珪素表面に形成され
た酸化珪素を捕らえるものと考える。即ち、金属珪素表
面に形成されている酸化珪素はおよそ1000℃以上
で、SiOとして気化し、SiOが離脱した直後の離脱
箇所の珪素は極めて高いエネルギー状態にあり、反応活
性が高まるが、反応源となる窒素は気体状で存在するた
め、急激なSiOガス量の増大に伴い系内での窒素分圧
が相対的に低下し、反応の進行が鈍化することがある。
更に、このSiOガスは窒素ガスよりも活性であり、加
熱中に加熱炉内のヒーター及び/又は炉壁材と反応する
ことが多々見られ、加熱後の冷却過程中で安定なSiO
2となってヒーター及び/又は炉壁材上に析出し易い。It is considered that the aluminum oxide in the present invention captures the silicon oxide formed on the surface of metallic silicon by the following actions. That is, the silicon oxide formed on the surface of the metallic silicon is vaporized as SiO at about 1000 ° C. or higher, and the silicon at the separation point immediately after the separation of SiO is in an extremely high energy state, and the reaction activity is increased. Since the nitrogen that is present in the form of gas exists in a gaseous state, the partial pressure of nitrogen in the system may relatively decrease with a rapid increase in the amount of SiO gas, and the reaction may slow down.
Furthermore, this SiO gas is more active than nitrogen gas, and it is often seen that it reacts with the heater and / or the furnace wall material in the heating furnace during heating, and the stable SiO gas is stable during the cooling process after heating.
It easily becomes 2 and precipitates on the heater and / or furnace wall material.
【0018】一方、この高温過程において、ヒーター及
び炉壁材よりも高い活性状態である酸化アルミニウム粉
末を共存させれば、SiOガスはヒーター及び炉壁材よ
りも酸化アルミニウム粉末との反応がより速やかに行わ
れ、また、SiO2化の酸素源も供給でき、かつSiO2
とAl2O3は安定な化合物や固溶体を形成しやすいこと
からも反応後のSiOガス再離脱はなく冷却過程下に至
るまで安定に留まらすことが出来る。更に酸化アルミニ
ウム粉末はヒーター及び炉壁材と比較し十分大きい表面
積を有するが故に、発生したSiOガスの全量と反応す
るに十分足り得る反応源となる。このように酸化アルミ
ニウム粉末は窒素ガスよりもSiOガスと速やかにかつ
優先的に反応し、炉内で未反応の残存SiOガス量を最
小限のレベルに留めることが出来る。On the other hand, in this high temperature process, if the aluminum oxide powder which is in a higher active state than the heater and the furnace wall material coexists, the SiO gas reacts with the aluminum oxide powder more quickly than the heater and the furnace wall material. done, also it can supply a source of oxygen SiO 2 reduction, and SiO 2
Since Al 2 O 3 and Al 2 O 3 easily form a stable compound or solid solution, there is no re-desorption of SiO gas after the reaction and it can remain stable until the cooling process. Further, since the aluminum oxide powder has a surface area which is sufficiently larger than that of the heater and the wall material of the furnace, it becomes a reaction source sufficient to react with the total amount of generated SiO gas. In this way, the aluminum oxide powder reacts with the SiO gas more quickly and preferentially than the nitrogen gas, and the amount of unreacted residual SiO gas in the furnace can be kept to a minimum level.
【0019】以上のことから、酸化アルミニウム粉末を
共存させれば、直接窒化による金属珪素の窒化反応も進
展し易く、また加熱炉内の炉材も殆ど汚染されずに、窒
化性雰囲気下に於いて表面に酸化物や酸窒化物が殆ど存
在しない高純度のα型窒化珪素粉末を安定かつ高い歩留
まりで得ることが出来る。From the above, the coexistence of the aluminum oxide powder facilitates the nitriding reaction of metallic silicon by direct nitriding, and the furnace material in the heating furnace is hardly contaminated, and the nitriding atmosphere is maintained. In addition, a high-purity α-type silicon nitride powder having almost no oxide or oxynitride on the surface can be obtained in a stable and high yield.
【0020】[0020]
【実施例】以下、実施例及び比較例によりこの発明を具
体的に詳しく説明する。 [実施例1] 表面部を中心に酸素2.0重量%(以下
特記無い限り%は全て重量%)と金属不純物0.2%を
含み、44μm以下の粒径からなる金属珪素粉末800
gを、厚さ1.2cmの反応焼結窒化珪素製の棚板4枚
に、それぞれ縦約15cm、横約25cm、厚さ約1c
mになるように200gずつ積載した。また、金属不純
物0.05%を含み、粒径50μm以下の酸化アルミニ
ウム粉末80gを前記と同様の反応焼結窒化珪素製の棚
板1枚の上に縦約15cm、横約25cm、最大厚さ約
0.5cmとなるように積載した。次いで加熱室内容積
0.05m3のバッチ式抵抗加熱炉の炉床から上におよ
そ5cmの間隔で5段に渡り前記各棚板を一枚づつ設置
可能な反応焼結窒化珪素製の支柱を組み、最下段に酸化
アルミニウムを積載した棚板を設置し、下から2段目か
ら5段目までに金属珪素を積載した棚板を各段に設置し
た。この設置状態の概略を図1に示す。EXAMPLES The present invention will be described in detail below with reference to Examples and Comparative Examples. Example 1 Metallic silicon powder 800 having a particle size of 44 μm or less, containing 2.0% by weight of oxygen (all% are% by weight unless otherwise specified) and 0.2% of metal impurities centered on the surface portion.
g to a shelf plate made of reaction-sintered silicon nitride having a thickness of 1.2 cm, each having a length of about 15 cm, a width of about 25 cm, and a thickness of about 1 c.
200 g each was loaded so as to be m. Further, 80 g of aluminum oxide powder containing 0.05% of metal impurities and having a particle size of 50 μm or less was placed on a shelf plate made of the same reaction-sintered silicon nitride as above, about 15 cm in length, about 25 cm in width, and maximum thickness. It was loaded so that it would be about 0.5 cm. Next, columns of reaction-sintered silicon nitride capable of installing the above-mentioned respective shelf plates one by one over 5 stages at intervals of approximately 5 cm above the hearth of a batch type resistance heating furnace having a heating chamber volume of 0.05 m 3 were assembled. A shelf board loaded with aluminum oxide was installed in the lowest stage, and a shelf board loaded with metallic silicon was installed in each of the second to fifth steps from the bottom. The outline of this installation state is shown in FIG.
【0021】[0021]
【図1】[Figure 1]
【0022】設置後、炉内雰囲気を純度99.99%の
窒素ガスで置換し、窒素雰囲気を約1気圧に保ち、昇温
速度が、室温〜1000℃迄を500℃/時、1000
〜1410℃迄を100℃/時、となるように加熱し、
1410℃で1時間保持した後、常温近傍まで炉内で自
然放冷した。冷却後、金属珪素粉末の窒化反応生成物に
対し、X線回折による定性及び定量分析を行った結果、
該反応生成物は、未反応残存珪素を0.2%、珪素以外
の金属不純物を0.1%を含む窒化珪素であり、そのα
化率は97%であった。また、少なくとも肉眼による観
察では加熱炉のヒーター、炉壁は変質しておらず、ヒー
ター、炉材上に新たな生成物も認められなかった。尚、
冷却後の酸化アルミニウム粉末からは粉末X線回折によ
り、Al2O3以外に等の当初不純物として含まれていた
以上のSiO2の存在が検出された他、微量のSi−A
l−O系化合物、及びSi−Al−O−N系化合物も検
出された。After the installation, the atmosphere in the furnace was replaced with nitrogen gas having a purity of 99.99%, the nitrogen atmosphere was maintained at about 1 atm, and the temperature rising rate was from room temperature to 1000 ° C at 500 ° C / hour, 1000 ° C.
Heat up to 1410 ° C to 100 ° C / hour,
After holding at 1410 ° C. for 1 hour, it was naturally cooled in the furnace to near room temperature. After cooling, the nitriding reaction product of the metallic silicon powder was subjected to qualitative and quantitative analysis by X-ray diffraction,
The reaction product is silicon nitride containing 0.2% of unreacted residual silicon and 0.1% of metal impurities other than silicon.
The conversion rate was 97%. Further, at least by visual observation, the heater of the heating furnace and the furnace wall were not deteriorated, and no new product was observed on the heater or the furnace material. still,
From the cooled aluminum oxide powder, the presence of SiO 2 other than Al 2 O 3 initially contained as impurities was detected by powder X-ray diffraction, and a small amount of Si-A
I-O type compounds and Si-Al-O-N type compounds were also detected.
【0023】[実施例2] 表面部を中心に酸素2.0
重量%(以下特記無い限り%は全て重量%)と金属不純
物0.2%を含み、44μm以下の粒径からなる金属珪
素粉末800gを、厚さ1.2cmの反応焼結窒化珪素
製の棚板4枚に、それぞれ縦約15cm、横約25c
m、厚さ約1cmになるように200gずつ積載した。
また、金属不純物0.05%を含み、粒径50μm以下
の酸化アルミニウム粉末80gを前記と同様の反応焼結
窒化珪素製の棚板1枚の上に縦約15cm、横約25c
m、最大厚さ約0.5cmとなるように積載した。次い
で加熱室内容積0.05m3のバッチ式抵抗加熱炉の炉
床から上におよそ5cmの間隔で5段に渡り前記各棚板
を一枚づつ設置可能な反応焼結窒化珪素製の支柱を組
み、最下段に酸化アルミニウムを積載した棚板を設置
し、下から2段目から5段目までに金属珪素を積載した
棚板を各段に設置した。設置後、炉内雰囲気を純度9
9.99%の窒素ガスで置換し、窒素雰囲気を約1気圧
に保ち、昇温速度が、室温〜1000℃迄を500℃/
時、1000〜1200℃迄を100℃/時、1200
〜1400℃迄を50℃/時、1400〜1500℃迄
を100℃/時、となるよう加熱し、1500℃到達後
直ちに常温近傍まで炉内で自然放冷した。冷却後、金属
珪素粉末の窒化反応生成物に対し、前記実施例1と同様
の分析を行った結果、該反応生成物は、未反応残存珪素
はなく、珪素以外の金属不純物を0.1%を含む窒化珪
素であり、そのα化率は97%であった。また、少なく
とも肉眼による観察では加熱炉のヒーター、炉材の変質
や新たな生成物も認められなかった。更に、冷却後の酸
化アルミニウム粉末からは粉末X線回折により、SiO
2、Si−Al−O系化合物、及びSi−Al−O−N
系化合物が検出された。[Example 2] Oxygen of 2.0 with the surface portion as the center
A rack made of reaction-sintered silicon nitride having a thickness of 1.2 cm, containing 800 g of metal silicon powder having a particle size of 44 μm or less and containing 0.2% by weight of metal impurities and 0.2% of metal impurities. Approximately 15 cm long and 25 c wide on each of the four plates
m and a thickness of about 1 cm, 200 g each was loaded.
Further, 80 g of aluminum oxide powder containing 0.05% of metal impurities and having a particle size of 50 μm or less was placed on a shelf plate of the same reaction sintered silicon nitride as above, about 15 cm in length and about 25 c in width.
m, and the maximum thickness was about 0.5 cm. Next, columns of reaction-sintered silicon nitride capable of installing the above-mentioned respective shelf plates one by one over 5 stages at intervals of approximately 5 cm above the hearth of a batch type resistance heating furnace having a heating chamber volume of 0.05 m 3 were assembled. A shelf board loaded with aluminum oxide was installed in the lowest stage, and a shelf board loaded with metallic silicon was installed in each of the second to fifth steps from the bottom. After installation, set the furnace atmosphere to a purity of 9
It is replaced with 9.99% nitrogen gas, the nitrogen atmosphere is kept at about 1 atm, and the temperature rising rate is 500 ° C / from room temperature to 1000 ° C.
Hour, 1000-1200 ℃ up to 100 ℃ / hour, 1200
Up to -1400 ° C. was heated to 50 ° C./hour, and from 1400 to 1500 ° C. was heated to 100 ° C./hour, and immediately after reaching 1500 ° C., it was naturally cooled in the furnace to near room temperature. After cooling, the nitriding reaction product of the metallic silicon powder was analyzed in the same manner as in Example 1. As a result, the reaction product was free of unreacted residual silicon and contained 0.1% of metal impurities other than silicon. Containing silicon nitride, and the α conversion rate was 97%. Further, at least by visual observation, neither the heater of the heating furnace nor the deterioration of the furnace material and new products were observed. Further, from the cooled aluminum oxide powder, powder X-ray diffraction was performed to obtain SiO.
2 , Si-Al-O-based compounds, and Si-Al-O-N
A system compound was detected.
【0024】[比較例1] 酸化アルミニウム粉末を設
置せずに、他の条件、手法は実施例2と同様にして作製
した金属珪素粉末の窒化反応生成物に対し、実施例2と
同様の分析を行ったところ、この反応生成物は、一部珪
素の溶融が見られ、未反応残存珪素を30%、珪素以外
の金属不純物を0.1%、更に酸窒化珪素(Si2O
N2)を0.05%それぞれ含む窒化珪素であり、その
α化率は80%であった。また、少なくとも肉眼による
観察では加熱炉のヒーター及び炉壁のほぼ全面に白色の
ファイバー状の物質が析出していた。この物質は棚板や
生成した窒化珪素粉末の一部表面にも析出が見られた。
この析出物を粉末X線回折により調べたところ、SiO
2が検出された。[Comparative Example 1] The same analysis as in Example 2 was performed on the nitriding reaction product of the metal silicon powder produced in the same manner as in Example 2 except that the aluminum oxide powder was not provided. In this reaction product, some of the silicon was melted, and unreacted residual silicon was 30%, metal impurities other than silicon were 0.1%, and silicon oxynitride (Si 2 O
N 2 ) was silicon nitride containing 0.05% of each, and the α conversion rate was 80%. Further, at least by visual observation, a white fiber-like substance was deposited on the heater of the heating furnace and almost the entire surface of the furnace wall. Precipitation of this material was also found on the surface of the shelf plate and a part of the generated silicon nitride powder.
When this precipitate was examined by powder X-ray diffraction, it was found that SiO
2 has been detected.
【0025】[比較例2] 酸化アルミニウム粉末を設
置する代わりに金属不純物0.05%を含み、粒径50
μm以下の窒化アルミニウム粉末80gを反応焼結窒化
珪素製の棚板1枚の上に縦約15cm、横約25cm、
厚さ約0.5cmとなるように積載したものを設置し、
他の条件、手法は実施例1と同様にして作製した金属珪
素粉末の窒化反応生成物に対し、前記実施例1と同様の
分析を行った結果、該反応生成物は、未反応残存珪素を
42%、珪素以外の金属不純物を0.1%を含む窒化珪
素であり、そのα化率は97%であった。また、少なく
とも肉眼による観察では加熱炉のヒーター及び炉壁のほ
ぼ全面に白色のファイバー状の物質が析出していた。こ
の物質は棚板や生成した窒化珪素粉末の一部表面にも析
出が見られた。この析出物を粉末X線回折により調べた
ところ、SiO2が検出された。COMPARATIVE EXAMPLE 2 Instead of installing aluminum oxide powder, 0.05% of metal impurities were contained and the particle size was 50.
80 g of aluminum nitride powder having a size of less than or equal to μm is placed on a shelf plate made of reaction-sintered silicon nitride to measure about 15 cm in length and about 25 cm in width
Install the loaded one so that the thickness is about 0.5 cm,
Other conditions and methods were the same as in Example 1 with respect to the nitriding reaction product of the metallic silicon powder produced in the same manner as in Example 1. As a result, the reaction product showed that unreacted residual silicon was present. It was silicon nitride containing 42% and 0.1% of metal impurities other than silicon, and its α conversion rate was 97%. Further, at least by visual observation, a white fiber-like substance was deposited on the heater of the heating furnace and almost the entire surface of the furnace wall. Precipitation of this material was also found on the surface of the shelf plate and a part of the generated silicon nitride powder. When this precipitate was examined by powder X-ray diffraction, SiO 2 was detected.
【図1】金属珪素粉末と酸化アルミニウム粉末を加熱炉
内に設置した説明図である。FIG. 1 is an explanatory diagram in which metallic silicon powder and aluminum oxide powder are installed in a heating furnace.
1 窒化性ガス送入口 2 ヒーター 3 ガス排出口弁 4 炉床 5 酸化アルミニウム粉末 6 金属珪素粉末 7 粉末積載用棚板 1 Nitriding Gas Inlet 2 Heater 3 Gas Outlet Valve 4 Hearth 5 Aluminum Oxide Powder 6 Metal Silicon Powder 7 Powder Loading Shelf Board
Claims (2)
触させずに共存させた酸化アルミニウム粉末と共に、窒
化性雰囲気中で加熱して成るα化率が96%以上で金属
不純物が0.4重量%以下であることを特徴とする窒化
珪素粉末。1. A metal silicon powder containing oxygen is heated in a nitriding atmosphere together with an aluminum oxide powder made to coexist without being brought into contact with the powder, and the α-conversion rate is 96% or more, and the metal impurities are 0.1. Silicon nitride powder characterized by being 4% by weight or less.
触させずに共存させた酸化アルミニウム粉末と共に、窒
化性雰囲気中で加熱して成るα化率が96%以上で金属
不純物が0.4重量%以下であることを特徴とする窒化
珪素粉末の製造方法。2. A metal silicon powder containing oxygen is heated together with an aluminum oxide powder coexisting without being in contact with the powder in a nitriding atmosphere to have an α-conversion rate of 96% or more and a metal impurity of 0.1. 4% by weight or less, a method for producing a silicon nitride powder.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7214173A JPH0948670A (en) | 1995-07-31 | 1995-07-31 | Silicon nitride powder and its production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7214173A JPH0948670A (en) | 1995-07-31 | 1995-07-31 | Silicon nitride powder and its production |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0948670A true JPH0948670A (en) | 1997-02-18 |
Family
ID=16651451
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP7214173A Pending JPH0948670A (en) | 1995-07-31 | 1995-07-31 | Silicon nitride powder and its production |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0948670A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2024195605A1 (en) * | 2023-03-22 | 2024-09-26 | デンカ株式会社 | Silicon nitride calcined body and production method therefor, and production method for silicon nitride powder |
-
1995
- 1995-07-31 JP JP7214173A patent/JPH0948670A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2024195605A1 (en) * | 2023-03-22 | 2024-09-26 | デンカ株式会社 | Silicon nitride calcined body and production method therefor, and production method for silicon nitride powder |
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