JPH0791044B2 - Method for producing easily sinterable silicon nitride powder - Google Patents
Method for producing easily sinterable silicon nitride powderInfo
- Publication number
- JPH0791044B2 JPH0791044B2 JP4743289A JP4743289A JPH0791044B2 JP H0791044 B2 JPH0791044 B2 JP H0791044B2 JP 4743289 A JP4743289 A JP 4743289A JP 4743289 A JP4743289 A JP 4743289A JP H0791044 B2 JPH0791044 B2 JP H0791044B2
- Authority
- JP
- Japan
- Prior art keywords
- silicon nitride
- powder
- nitride powder
- temperature
- easily sinterable
- 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
- 239000000843 powder Substances 0.000 title claims description 57
- 229910052581 Si3N4 Inorganic materials 0.000 title claims description 29
- HQVNEWCFYHHQES-UHFFFAOYSA-N silicon nitride Chemical compound N12[Si]34N5[Si]62N3[Si]51N64 HQVNEWCFYHHQES-UHFFFAOYSA-N 0.000 title claims description 29
- 238000004519 manufacturing process Methods 0.000 title claims description 5
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 14
- 229910052814 silicon oxide Inorganic materials 0.000 claims description 11
- 230000001590 oxidative effect Effects 0.000 claims description 4
- 238000002156 mixing Methods 0.000 claims description 3
- 238000000034 method Methods 0.000 description 15
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 12
- 239000001301 oxygen Substances 0.000 description 12
- 229910052760 oxygen Inorganic materials 0.000 description 12
- 238000010438 heat treatment Methods 0.000 description 7
- 239000002245 particle Substances 0.000 description 7
- 238000005452 bending Methods 0.000 description 6
- 239000010419 fine particle Substances 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 3
- 238000000465 moulding Methods 0.000 description 3
- 238000005121 nitriding Methods 0.000 description 3
- 238000005245 sintering Methods 0.000 description 3
- 239000007858 starting material 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
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- -1 silicon halide Chemical class 0.000 description 2
- 238000012546 transfer 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
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 1
- 238000007088 Archimedes method Methods 0.000 description 1
- 229910004298 SiO 2 Inorganic materials 0.000 description 1
- 238000002441 X-ray diffraction Methods 0.000 description 1
- 239000004964 aerogel Substances 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000011362 coarse particle Substances 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000011835 investigation Methods 0.000 description 1
- 239000011812 mixed powder Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 238000002407 reforming Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- LIVNPJMFVYWSIS-UHFFFAOYSA-N silicon monoxide Chemical compound [Si-]#[O+] LIVNPJMFVYWSIS-UHFFFAOYSA-N 0.000 description 1
- 239000006104 solid solution Substances 0.000 description 1
- 238000000859 sublimation Methods 0.000 description 1
- 230000008022 sublimation Effects 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
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- 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、軸受等に利用される窒化ケイ素粉末特に易焼結性
で且つ高温強度を発現する窒化ケイ素粉末の製造方法に
関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial field of application] The present invention relates to a silicon nitride powder used as a high-temperature structural material for a gas turbine member, a nozzle, a bearing, etc., particularly, it is easily sinterable and exhibits high-temperature strength. The present invention relates to a method for producing silicon nitride powder.
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
素量或いは粒径、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多きな
違いがある。Conventionally, as methods for producing silicon nitride powder, (1) direct metal nitriding method, (2) silica reduction nitriding method, and (3) silicon halide method are known. Probably because the powders produced by these methods have different production 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 are many differences 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, and the powder of the method (2) is hardly sinterable but has high high-temperature bending strength, The powder of the method (3) is said to exhibit intermediate performance.
特に、(1)の方法で製造された窒化ケイ素粉末は他の
2法に比べて粉砕に伴う歪を粉体の表面で受けているの
で、その歪エネルギーを解放してやることにより何んら
かの特徴を粉体に与えることの研究がなされている。そ
の1例が特開昭53−88011号公報である。In particular, since the silicon nitride powder produced by the method (1) receives strain due to pulverization on the surface of the powder as compared with the other two methods, it is possible to release some strain energy by releasing the strain energy. Research has been done on imparting characteristics to powders. One example is JP-A-53-88011.
この先行技術は、窒化ケイ素粉末を1,400〜1,900℃の温
度で加熱処理し、窒化ケイ素中に含まれている酸素をSi
Oとして除去すると共に、一部の酸素を窒化ケイ素粉体
の表面に固溶せしぬ、焼結助剤とのぬれ性を改善するこ
とにより焼結体中の粒界相の量を減少せしめる技術であ
り、その結果、高温高強度が発現するというものであ
る。In this prior art, silicon nitride powder is heat-treated at a temperature of 1,400 to 1,900 ° C. to remove oxygen contained in silicon nitride into Si.
The amount of the grain boundary phase in the sintered body can be reduced by removing it as O and not dissolving a part of oxygen on the surface of the silicon nitride powder as a solid solution and improving the wettability with the sintering aid. It is a technology, and as a result, high temperature and high strength are developed.
しかし、この方法は、出発原料の窒化ケイ素粉体の表面
における物質移動を利用したものであるので、自ずと出
発原料が限定される、すなわち、微粉か又は高酸素の原
料であることが要求されるという問題がある。従つて、
粉体の改質にも限度があり、その結果の1例がホツトプ
レスのみの使用であつて、完全に粉体特性を把握できな
かつた点に問題が残されていた。However, since this method utilizes mass transfer on the surface of the silicon nitride powder as the starting material, the starting material is naturally limited, that is, it is required to be a fine powder or a material with high oxygen content. There is a problem. Therefore,
There is a limit to the modification of powder, and one example of the results is the use of only hot press, which leaves a problem in that the powder characteristics could not be completely grasped.
本発明者らは、特開昭53−88011号公報における以上の
問題点を念願に入れ、粉体改良の方法と改良された粉体
の結ひつきを種々検討した結果、出発原料にこだわるこ
となく窒化ケイ素粉末にケイ素酸化物微粉を添加混合
し、非酸化性雰囲気下、1,500〜1,800℃の温度で熱処理
をすれば常圧焼結にも適用可能な粉体となることを見い
出し、本発明を完成した。In view of the above problems in JP-A-53-88011, the present inventors have made various investigations on the method of improving powder and the binding of improved powder, and as a result, stick to the starting material. It was found that if powder of silicon oxide is added to and mixed with silicon nitride powder without heat treatment and heat-treated at a temperature of 1,500 to 1,800 ° C. under a non-oxidizing atmosphere, the powder can be applied to atmospheric pressure sintering. Was completed.
すなわち、本発明は、窒化ケイ素粉末にケイ素酸化物微
粉を添加混合し、非酸化性雰囲気下、1,500〜1,800℃の
温度で熱処理することを特徴とする易焼結性窒化ケイ素
粉末の製造方法である。That is, the present invention is a method for producing an easily sinterable silicon nitride powder characterized by adding and mixing silicon oxide fine powder to silicon nitride powder, and heat-treating at a temperature of 1,500 to 1,800 ° C. under a non-oxidizing atmosphere. is there.
以下、さらに詳しく本発明について説明すると、本発明
において、ケイ素酸化物微粉を添加する理由は、窒化ケ
イ素粉末中の酸素が微粉に偏ると窒化ケイ素粉体の表面
改質が微粉のみで行われ、酸素の少ないと考えられる粗
粒例えば5〜10μm程度の粉末が改質から取り残される
恐れがあることに鑑みたものである。すなわち、本発明
では、積極的にケイ素酸化物微粉を添加し窒化ケイ素粉
体の表面と反応させることによりこの問題を解消しよう
とするものである。Hereinafter, the present invention will be described in more detail.In the present invention, the reason for adding the silicon oxide fine powder is that the surface modification of the silicon nitride powder is performed only by the fine powder when oxygen in the silicon nitride powder is biased to the fine powder, This is because coarse particles that are considered to have a small amount of oxygen, for example, powder having a particle size of about 5 to 10 μm may be left behind from the reforming. That is, the present invention intends to solve this problem by positively adding fine silicon oxide powder and reacting with the surface of the silicon nitride powder.
ケイ素酸化物の添加量は、以下の目的と原料窒化ケイ素
粉末の酸素を考慮して決定されるが、通常は6重量%以
内である。すなわち、その目的の1つは、易焼結性を付
与した粉体の改良であつて、他の1つは低酸素化及び微
粉同士の再配列化である。前者は、ケイ素酸化物微粉を
2重量%以内の添加とし、比較的低温例えば1600℃程度
までの温度で熱処理を行つて粉体表面のぬれ性を改善し
ようとするものである。一方、後者は、特願昭63−2773
60号明細書の技術内容を狙つたものであつて、高温例え
ば1750℃程度の熱処理であつて、ケイ素酸化物微粉も出
来るだけ多く添加し、積極的に反応せしめ、脱酸素を行
い、低酸素化は勿論のこと、微粉同士の再配列化も行
い、微粉を減少させようとするものである。熱処理時間
としては温度にも影響するが3〜15時間程度であれば十
分である。The amount of silicon oxide added is determined in consideration of the following purposes and oxygen of the raw material silicon nitride powder, but is usually within 6% by weight. That is, one of the purposes is to improve the powder having easy sinterability, and the other is to reduce oxygen and rearrange fine powders. The former is intended to improve the wettability of the powder surface by adding the fine powder of silicon oxide within 2% by weight and performing heat treatment at a relatively low temperature, for example, at a temperature up to about 1600 ° C. On the other hand, the latter is the Japanese Patent Application No. 63-2773.
Aiming at the technical contents of No. 60 specification, it is a heat treatment at a high temperature, for example, about 1750 ° C., and as much silicon oxide fine powder as possible is added, and the reaction is positively carried out to perform deoxidation and low oxygen content. In addition to the formation of fine particles, the fine particles are rearranged to reduce the fine particles. The heat treatment time also affects the temperature, but about 3 to 15 hours is sufficient.
ケイ素酸化物の粒度は、前述のように、積極的に窒化ケ
イ素粉体の表面と反応させることを目的としているので
小さい方が好ましい。具体的には原料窒化ケイ素粉末の
比表面積より大きいことが望ましく、10m2/g以上の微粉
であることが好都合である。このようなケイ素酸化物微
粉の具体例としてはアエロジエル、ホワイトカーボン等
があげられる。As described above, the particle size of the silicon oxide is preferably smaller because it is intended to positively react with the surface of the silicon nitride powder. Specifically, it is desirable that the specific surface area of the raw material silicon nitride powder be larger, and it is convenient that the fine powder is 10 m 2 / g or more. Specific examples of such fine particles of silicon oxide include aerogel, white carbon and the like.
熱処理の雰囲気については、低酸素化を目的にしている
ので、非酸化性雰囲気下、例えば、窒素,アルゴン,水
素,アンモニア等の雰囲気が好適である。また、熱処理
温度については1,500〜1,800℃が最適である。1,500℃
未満であるとケイ素酸化物微粉と窒化ケイ素粉体との反
応すなわち物質移動が十分に起こらないで粉体の改質が
できない。一方、1,800℃を越えると窒化ケイ素自身の
昇華転移及び一部分解が生じる。The heat treatment atmosphere is preferably a non-oxidizing atmosphere, for example, an atmosphere of nitrogen, argon, hydrogen, ammonia, or the like, for the purpose of reducing oxygen. The optimum heat treatment temperature is 1,500-1,800 ° C. 1,500 ° C
If it is less than the range, the reaction between the silicon oxide fine powder and the silicon nitride powder, that is, the mass transfer does not sufficiently occur, and the powder cannot be modified. On the other hand, when the temperature exceeds 1,800 ° C, sublimation transition and partial decomposition of silicon nitride itself occur.
以上、詳しく説明したように、本発明は、窒化ケイ素粉
末特に直接窒化法で得られた窒化ケイ素粉末の欠点例え
ば酸素を多く含んでいる等の欠点をケイ素酸化物微粉を
積極的に添加して易焼結性と高温強度の発現が容易な窒
化ケイ素粉末に改質したものであり、本発明の基本思想
は、下記(1)式及び(2)式に示す反応にもとづいて
いる。As described above in detail, the present invention has the disadvantages of silicon nitride powder, particularly silicon nitride powder obtained by the direct nitriding method. The silicon nitride powder is modified to easily sinter and develop high-temperature strength. The basic idea of the present invention is based on the reactions shown in the following formulas (1) and (2).
α−Si3N4+SiO2→2Si2ON2 (1) 2Si2ON2→β−Si3N4+SiO↑ (2) 〔実施例〕 以下、実施例と比較例をあげてさらに具体的に本発明を
説明する。α-Si 3 N 4 + SiO 2 → 2Si 2 ON 2 (1) 2Si 2 ON 2 → β-Si 3 N 4 + SiO ↑ (2) [Example] Hereinafter, more specific examples and comparative examples will be given. The present invention will be described.
実施例1〜11,比較例1〜4 市販品の窒化ケイ素粉末100重量部に非表面積50m2/gのS
iO2を第1表に示す割合で添加混合した。この混合粉末
をカーボンルツボに入れ、第1表に示す熱処理条件で加
熱し、窒化ケイ素粉末を製造した。得らた窒化ケイ素粉
末の特性を第1表に示す。Examples 1 to 11 and Comparative Examples 1 to 4 100 parts by weight of a commercially available silicon nitride powder is used, and S having a non-surface area of 50 m 2 / g is added.
iO 2 was added and mixed at a ratio shown in Table 1. This mixed powder was put into a carbon crucible and heated under the heat treatment conditions shown in Table 1 to produce a silicon nitride powder. The characteristics of the obtained silicon nitride powder are shown in Table 1.
次に、以上のように熱処理して得られた窒化ケイ素粉末
に、Y2O3(平均粒子径1.3μm)、Al2O3(平均粒子径1.
4μm)、MgO(平均粒子径1.2μm)及びMgO・Al2O
3(平均粒子径1.2μm)を第2表に示すように種々の割
合で内割配合し、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
密度及び常温(δRT)と1200℃(δ1200)の曲げ強度を
測定した。その結果を第3表に示す。 Next, Y 2 O 3 (average particle diameter of 1.3 μm) and Al 2 O 3 (average particle diameter of 1.
4 μm), MgO (average particle size 1.2 μm) and MgO ・ Al 2 O
As shown in Table 2, 3 (average particle size 1.2 μm) was internally blended in various proportions, and 1,1,1-trichloroethane was added to give 4
After wet mixing with a ball mill for 2 hours, dry and mold with a molding pressure of 100 kg / cm 2 into a 6 × 10 × 60 mm shape, then 2700 kg / cm 2
CIP molding was performed at the molding pressure of. 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 grinding the obtained sintered body, the relative density and bending strength at room temperature (δ RT ) and 1200 ° C (δ 1200 ) were measured. The results are shown in Table 3.
なお第1表と第3表に示した測定値は次の方法によつ
た。 The measured values shown in Tables 1 and 3 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 type 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 BET1点法による。(2) Specific surface area (m 2 / g): According to Cantersorb Jr BET 1-point method manufactured by Yuasa Ionics.
(3)α分率(%):理学電機社製のガイガーフラツク
スRAD−II B型のX線回折による。(3) α fraction (%): by X-ray diffraction of Geiger Frax RAD-II B type manufactured by Rigaku Denki KK
(4)相対密度(%):アルキメデス法による。(4) Relative density (%): By Archimedes method.
(5)曲げ強度(MPa):島津製作所製オートグラフAG
−2000A型による。(5) Bending strength (MPa): Autograph AG manufactured by Shimadzu
-By type 2000A.
本発明により製造された窒化ケイ素粉末は、低酸素にも
かわらず易焼結性であり、1200℃における高温曲げ強度
が800MPa以上可能となる。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。The silicon nitride powder produced by the present invention is easily sinterable in spite of low oxygen content, and high temperature bending strength at 1200 ° C. can be 800 MPa or more. This is a result of controlling the powder properties related to the generation and growth of β-columnar crystals in the sintered body.
Claims (1)
混合し、非酸化性雰囲気下、1,500〜1,800℃の温度で熱
処理することを特徴とする易焼結性窒化ケイ素粉末の製
造方法。1. A method for producing an easily sinterable silicon nitride powder, which comprises adding and mixing fine silicon oxide powder to silicon nitride powder and heat-treating at a temperature of 1,500 to 1,800 ° C. in a non-oxidizing atmosphere.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4743289A JPH0791044B2 (en) | 1989-02-28 | 1989-02-28 | Method for producing easily sinterable silicon nitride powder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4743289A JPH0791044B2 (en) | 1989-02-28 | 1989-02-28 | Method for producing easily sinterable silicon nitride powder |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH02225306A JPH02225306A (en) | 1990-09-07 |
| JPH0791044B2 true JPH0791044B2 (en) | 1995-10-04 |
Family
ID=12774991
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4743289A Expired - Fee Related JPH0791044B2 (en) | 1989-02-28 | 1989-02-28 | Method for producing easily sinterable silicon nitride powder |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0791044B2 (en) |
-
1989
- 1989-02-28 JP JP4743289A patent/JPH0791044B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH02225306A (en) | 1990-09-07 |
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