JPH0465003B2 - - Google Patents
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- Publication number
- JPH0465003B2 JPH0465003B2 JP3663387A JP3663387A JPH0465003B2 JP H0465003 B2 JPH0465003 B2 JP H0465003B2 JP 3663387 A JP3663387 A JP 3663387A JP 3663387 A JP3663387 A JP 3663387A JP H0465003 B2 JPH0465003 B2 JP H0465003B2
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- JP
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- powder
- carbon
- boehmite
- source material
- carbon source
- Prior art date
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- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 76
- 229910052799 carbon Inorganic materials 0.000 claims description 69
- 239000000843 powder Substances 0.000 claims description 51
- 229910001593 boehmite Inorganic materials 0.000 claims description 44
- FAHBNUUHRFUEAI-UHFFFAOYSA-M hydroxidooxidoaluminium Chemical compound O[Al]=O FAHBNUUHRFUEAI-UHFFFAOYSA-M 0.000 claims description 44
- 239000000463 material Substances 0.000 claims description 31
- 239000007787 solid Substances 0.000 claims description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 14
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 12
- 238000004519 manufacturing process Methods 0.000 claims description 10
- 238000002156 mixing Methods 0.000 claims description 9
- 239000012298 atmosphere Substances 0.000 claims description 7
- 230000001590 oxidative effect Effects 0.000 claims description 7
- 229910052757 nitrogen Inorganic materials 0.000 claims description 6
- 238000010304 firing Methods 0.000 claims description 5
- PMHQVHHXPFUNSP-UHFFFAOYSA-M copper(1+);methylsulfanylmethane;bromide Chemical compound Br[Cu].CSC PMHQVHHXPFUNSP-UHFFFAOYSA-M 0.000 claims description 4
- 238000001035 drying Methods 0.000 claims description 3
- 239000007788 liquid Substances 0.000 claims description 2
- 239000002245 particle Substances 0.000 description 26
- 238000000034 method Methods 0.000 description 19
- 239000000203 mixture Substances 0.000 description 17
- 239000006185 dispersion Substances 0.000 description 10
- 238000005121 nitriding Methods 0.000 description 10
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 9
- 238000009826 distribution Methods 0.000 description 9
- 230000000052 comparative effect Effects 0.000 description 6
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 5
- 238000006243 chemical reaction Methods 0.000 description 5
- 230000002829 reductive effect Effects 0.000 description 5
- WNROFYMDJYEPJX-UHFFFAOYSA-K aluminium hydroxide Chemical compound [OH-].[OH-].[OH-].[Al+3] WNROFYMDJYEPJX-UHFFFAOYSA-K 0.000 description 4
- 239000012535 impurity Substances 0.000 description 4
- 238000004898 kneading Methods 0.000 description 4
- 239000013078 crystal Substances 0.000 description 3
- 238000005261 decarburization Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000001879 gelation Methods 0.000 description 3
- 239000002904 solvent Substances 0.000 description 3
- 239000003513 alkali Substances 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 2
- 239000010419 fine particle Substances 0.000 description 2
- 230000007062 hydrolysis Effects 0.000 description 2
- 238000006460 hydrolysis reaction Methods 0.000 description 2
- 230000001788 irregular Effects 0.000 description 2
- 238000006386 neutralization reaction Methods 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 238000005245 sintering Methods 0.000 description 2
- 239000007858 starting material Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- LSNNMFCWUKXFEE-UHFFFAOYSA-M Bisulfite Chemical compound OS([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-M 0.000 description 1
- 229910004298 SiO 2 Inorganic materials 0.000 description 1
- 238000002441 X-ray diffraction Methods 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 150000004703 alkoxides Chemical class 0.000 description 1
- AZDRQVAHHNSJOQ-UHFFFAOYSA-N alumane Chemical class [AlH3] AZDRQVAHHNSJOQ-UHFFFAOYSA-N 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- -1 aluminum alkoxide Chemical class 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 150000001721 carbon Chemical class 0.000 description 1
- 239000002270 dispersing agent Substances 0.000 description 1
- 238000010292 electrical insulation Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000008394 flocculating agent Substances 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 230000017525 heat dissipation Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000003779 heat-resistant material Substances 0.000 description 1
- 239000008241 heterogeneous mixture Substances 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 229920005610 lignin Polymers 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 239000012299 nitrogen atmosphere Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000001935 peptisation Methods 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 229910052573 porcelain Inorganic materials 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- 230000001568 sexual effect Effects 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 239000010409 thin film Substances 0.000 description 1
Landscapes
- Ceramic Products (AREA)
Description
〔産業上の利用分野〕
本発明は、高純度、微細で易焼結性の窒化アル
ミニウム粉末の製造方法に関するものである。
〔従来の技術〕
窒化アルミニウム(以下AlNと記す)は、そ
の優れた機械的特性、化学的耐用性の故に耐熱材
料として用いられるだけでなく、その高熱伝導
性、高電気絶縁性、低誘電率等の故に半導体関係
の放熱材料としても期待されている。AlNは一
部薄膜の形態で利用される場合もあるが、多くの
場合焼結体で用いられている。
このようなAlN焼結体の焼結性および特性は、
出発原料であるAlN粉末の特性および焼結助剤
に強く影響されることが知られている。すなわ
ち、AlN粉末としては、高純度で、粒径が均一
かつ微細であり、適当な焼結助剤がAlN粉中に
均一に分散していることが望ましい。
AlN粉末は、従来、金属アルミニウムの直接
窒化法またはアルミナの還元窒化法で製造されて
いる。直接窒化法では微細で均一粒径の高純度ア
ルミナを出発原料とすることにより直接窒化法に
より若干優れたAlN粉末が得られやすいが、所
望の粉末とは言い難い。
上記方法を改良し、高純度で、微細、均一粒径
のAlN粉末を得る方法として、アルミニウムア
ルコキシドと炭素の分散液に水を加え、アルコキ
シドの加水分解を行わせ、水酸化アルミニウムと
炭素の混合物を得る方法、および水溶性アルミニ
ウム塩と炭素を含む水溶液にアルカリを加え、中
和沈殿法により水酸化アルミニウムと炭素の混合
物を得る方法が提案されている(特開昭61−
6105、特公昭61−26485)。
これらの方法によつて得た混合物は、前記した
アルミナと炭素の混合物に比べ均一に混合されて
いるため、これを窒素を含む非酸化性雰囲気中で
焼成することにより、従来より均一で、微細な
AlN粉を得ることができるようになつた。
しかし、上記の改良法においても加水分解また
は中和沈殿のために水またはアルカリを滴下する
と、局所的に沈殿が生成し、直ちに凝集してしま
う。このため、炭素微粉を含まない水酸化アルミ
ニウムの1μm以上の凝集塊が多数生成し、得られ
る水酸化アルミニウムと炭素の混合物は均一性が
不十分なものである。このような不均一な混合物
を窒素を含む非酸化性雰囲気中で焼成して得られ
るAlN粉の粒径も不揃いなものになり易く、焼
成後もアルミナが窒化されずに残つたり1〜5μm
の粗粒のAlNとなりがちであつた。
以上の問題点を解決するために、本発明者らは
特願昭61−05863において分散性、分散液の安定
性に優れるベーマイト(AlOOH)または凝ベー
マイト粉を用い、炭素源物質との均一な分散液を
作製し、この均一分散状態を保つたまま固化さ
せ、これを乾燥、焼成することによつて微細で粒
度分布範囲の狭いAlN粉を得る方法を開示した。
上記開示において、固体炭素を炭素源として用
いる場合には、その粒径および分散状態によつ
て、得られるAlN粉末の粒径分布が変動し易く、
例えば粒径が1μmを超える大きさとなつたり、ま
た分散が不十分な場合には1μm以上の凝結した
AlN粒が多数認められたり、極端な場合には窒
化が不十分でアルミナが残存する場合もあつた。
〔発明が解決しようとする問題点〕
本発明は高純度で微細な、焼結性にすぐれた
AlN粉末の製造法に関する上記開示をさらに発
展させ、優れたAlN粉末の品質をさらに向上さ
せ、粒度分布範囲が狭く、微細AlN粉を安定的
に再現性よく製造する方法を提供することを目的
とするものである。
〔問題点を解決するための手段〕
高純度で微細な、優れた焼結体を有するAlN
粉末を安定に、再現性よく製造する方法として、
本発明は次の技術手段から成る。
(1) 水中で極めて分散性に優れるベーマイトまた
は凝ベーマイト粉を水に加え、PHを1.2〜4.5の
範囲に調整することにより、ベーマイトが安定
に分散したベーマイトゾルをあらかじめ作製す
る。ベーマイトゾル中のベーマイト粒子径は
500Å以下である。凝ベーマイトは、ベーマイ
ト結晶と同位置にX線回折ピークがあらわれる
が、ベーマイト結晶に比べ、ピーク幅が広く、
結晶の不十分なベーマイトであるが、水中の分
散性の点でベーマイト結晶と大差はない。
(2) 上記ベーマイトゾルに加える炭素源物質とし
て、水溶性の有機炭素源物質から得られる炭素
と固体炭素粉とをその重量比が0.05〜0.5の範
囲になるように有機炭素源物質と固体炭素を配
合した炭素源物質を用いる。この固体炭素粉は
粒径0.5μm以下が好ましい。
この炭素源物質中の全炭素量とベーマイトと
を重量比で0.4〜3.0の割合で均一に混合したの
ち、この均一混合状態を保持したまま固化さ
せ、乾燥したのち、窒素を含む非酸化性雰囲気
中で焼成する。
(3) 上記(2)の工程において、ベーマイトゾルと炭
素源物質の分散体の均一混合状態をそのまま保
持し固化させるために、蒸発等によつて水を除
き、ベーマイトゾルを炭素と共存させたままゲ
ル化させ、次いで乾燥した後、窒素を含む非酸
化性雰囲気中で焼成することが好ましい。
ここで、水溶性の有機炭素源物質としては、水
溶性のレジン、リグニンスルホン酸など、ベーマ
イトゾルの分散性に影響を与えず、かつ高温での
炭素残留率の高いものが望ましい。
〔作 用〕
本発明を作用と共に具体的に説明する。
まず、ベーマイト粉または凝ベーマイト粉を水
に加え、ベーマイトゾルの分散状態が最適となる
ようにPH=1.2〜4.5の範囲に調整する。
次に、水溶性の有機炭素源物質から得られる炭
素と固体炭素微粉とをその重量比が0.05〜0.5の
範囲になるように配合して炭素源物質を調整し、
この炭素源物質中の全炭素量とベーマイト粉とが
重量比で、0.4〜3.0の割合となるように、前記ベ
ーマイトゾルと炭素源物質とを均一に混合する。
この混合物を均一混合状態を保持したまま固化さ
せ、乾燥させた後、窒素を含む非酸化性雰囲気中
で1350〜1700℃で焼成してAlN粉を得る。
上記混合物を固化させる手段としては、次の3
通りが代表的である。
イ) 長時間混練を続ける。混練中にベーマイト
ゾルのゲル化が々に進行するため、混合物の粘
度が時間とともに徐々に上昇し固化する。
ロ) 混練しながら加熱等によつて水を強制的に
揮散させ、ゲル状態にする。
ハ) 酸、アルカリ、種々のイオン、高分子凝集
剤などの添加によつてゲル化を促進させる。
ベーマイトゾルの作製において、PHを1.2〜4.5
の範囲に限定したのは、以下の理由による。PHが
1.2未満ではベーマイトゾルのゲル化が急速に進
むことにより、炭素源物質との混合操作を実質上
行うことができない。PHが4.5を超えるとベーマ
イト粉は水中に分散されず、1μm以上の凝集塊の
まま存在するため、炭素源物質との均一混合が難
しい。
炭素源物質として、水溶性の有機炭素源物質か
ら得られる炭素と固体炭素微粉とを、その重量比
が0.05〜0.5の範囲になるように配合するのは以
下の理由による。
本発明の効果は、炭素源物質とベーマイトゾル
を極限まで均一に混合することによつて最大限達
成される。これらの均一混合のためには、まずベ
ーマイトと炭素が均一に分散された状態を作り出
す必要がある。
ベーマイトは上記のように水のPHを調整するこ
とにより、良分散体が得られる。一方、炭素源物
質の良分散体を得る方法としては、微粉の固体炭
素を溶媒中に解膠、分散させる方法、または溶媒
(本発明の場合の溶媒は水)に溶解する有機炭素
源物質を用いる方法がある。炭素源物質として固
体炭素粉のみを用いた場合には、たとえ微粉の固
体炭素のみを使用しても通常の場合粒径は200Å
以上であり、かつこの微粉炭素を極限まで解膠、
分散させることは難しい。このため、ベーマイト
粒の周囲を固体炭素で覆うためには極めて多量の
固体炭素が必要であり、AlN粉末の生産効率は
極めて低いものとなつてしまう。また、固体炭素
の解膠、分散が少しでも不十分な場合にはベーマ
イトが還元窒化されずにアルミナとして残つた
り、得られるAlN粉末の粒径が不揃いになり易
く、品質の安定性、再現性の面からも好ましくな
い。
この問題を解決するためには、炭素の均一分散
が容易な水溶性有機炭素源物質を用いることが有
効である。ただ、有機炭素源物質を多量に使用す
ると、AlN粉合成時の高温過程で炭素と炭素と
の間の結合が強固に形成され、ベーマイトの環元
窒化反応後AlNと炭素の結合した極めて硬い塊
状物となつてしまう。
すなわちAlNと炭素との混合物を酸化性雰囲
気中で処理し、AlN粉の酸化を抑えながら脱炭
するためには上記塊状物を予めできるだけ細かく
粉砕しておくことが重要である。塊状物が必要以
上に硬い場合には粉砕に長時間を要するだけでな
く、粉砕時に不純物の混入が避けられないほか、
残留炭素分も多くなる。
以上の理由から、有機炭素源物質から得られる
炭素と固体炭素粉との比が0.05未満の場合には添
加の効果が実質的に認められない程小さく、また
この比が0.5を超えると還元化反応後のAlNと炭
素との塊状物が極めて硬くなつてしまうので、
0.05〜0.5に規制される。
炭素源物質中の全炭素量とベーマイト粉との混
合重量比を0.4〜3.0の範囲に限定したのは以下の
理由による。
重量比が0.4未満の場合には還元窒化後でもア
ルミナが残存するほか、粒径も大きくなる。重量
比が3.0を超えるとAIN粉末の生産効率が極めて
低くなり、実際的でない。
本発明によれば、微細で(1μm以下)、粒径分
布の極めて狭いAlN粉を安定に、再現性よく製
造することができる。
本発明は以下の2点において、先行技術をさら
に改良したものである。
(a) 水溶性有機炭素源物質を適量配合したため、
平均粒径がより小さく、粒径分布もより狭くな
つて成形性、焼結性がより向上した。
(b) 先行出願で炭素の分散状態が得られるAlN
粉の性状に極めて敏感に大きく影響する。これ
に対して本発明では製造ばらつきが小さい。
本発明のAlN粉は、原料ベーマイトとして高
純度のものを用いることにより容易に高純度化す
ることができ、例えば金属イオン総不純物量が
200ppm以下の純度のものを容易に得ることがで
きる。
さらに、本発明では微細なベーマイト粉と炭素
粉を均一に混合しているため、還元窒化時に
F2O3,SiO2などの不純物が容易に還元、揮散さ
れ、その結果さらに高純度のAlN粉を得ること
ができる。また、本発明のAlN粉を用いること
により、高純度で緻密(密度99%以上)な焼結体
を容易に得ることができる。
〔実施例〕
第1表に示した〜の配合でAlN製造用の
混合物を作製し、窒素雰囲気中で1450℃、5時間
焼成したのち、650℃で3時間脱炭処理し、AlN
粉を得た。
第1表中、、、は本発明の製造条件に
適合する実施例であり、、、、、は比
較例である。これらの全てについて以下の手順で
混合物を作成した。
PH=3.0で分散させた20重量%ベーマイトゾル
と、固体炭素に分散剤と水を加えポツトミルで10
時間混練して得た炭素15重量%分散体とを予め作
成する。両者を混合したのち、水溶性有機炭素源
物質を所定量添加する。添加後のこの混合物を撹
拌しながら、加熱によつて水を除去し、ゲル化さ
せた後、乾燥する。
上記〜の9種類のAlN粉の粒度分布を第
1図に、窒化反応後および脱炭後のAl2O3および
炭素含量を第2表に示す。第1図中および第2表
中の〜は第1表中の〜とそれぞれ対応す
る。
第1図、第2表から以下のことを確認すること
ができた。
比較例、は粒径が粗く、AlN中のAlBO3
残量も実施例、、、に比べて多い。ま
た、得られたAlN粉の粒径分布、Al2O3含量とも
製造ロツト間でばらつき易い。
実施例、、、は比較例、に比べ、
粒径が細かく、粒度分布が狭く、かつロツト間の
ばらつきも小さい。脱炭後のAl2O3残量、炭素残
量も少ない。
比較例、では窒化反応後の塊状物が硬すぎ
るため、粉砕時に不純物が混入し易い。アルミナ
磁器を用いた場合でも粉砕によりAl2O3含量が増
加している(第2表)。
また、比較例、は脱炭後の炭素残量も多
い。
比較例では窒化反応後にAl2O3が多量に残る
ほか、AlN粉の粒径も粗い。
[Industrial Application Field] The present invention relates to a method for producing highly pure, fine, easily sinterable aluminum nitride powder. [Prior Art] Aluminum nitride (hereinafter referred to as AlN) is not only used as a heat-resistant material because of its excellent mechanical properties and chemical durability, but also because of its high thermal conductivity, high electrical insulation, and low dielectric constant. For these reasons, it is also expected to be used as a heat dissipation material for semiconductors. Although AlN is sometimes used in the form of a thin film, it is often used in the form of a sintered body. The sinterability and properties of such AlN sintered bodies are
It is known that this is strongly influenced by the properties of the starting material AlN powder and the sintering aid. That is, it is desirable that the AlN powder has high purity, uniform and fine particle size, and that an appropriate sintering aid is uniformly dispersed in the AlN powder. AlN powder has conventionally been produced by direct nitriding of metal aluminum or reductive nitriding of alumina. In the direct nitriding method, by using high purity alumina with fine and uniform particle size as the starting material, it is easier to obtain a slightly better AlN powder by the direct nitriding method, but it is difficult to say that it is the desired powder. As a method to improve the above method and obtain AlN powder with high purity, fine, and uniform particle size, water is added to a dispersion of aluminum alkoxide and carbon to cause hydrolysis of the alkoxide, and a mixture of aluminum hydroxide and carbon is produced. A method for obtaining a mixture of aluminum hydroxide and carbon by adding an alkali to an aqueous solution containing a water-soluble aluminum salt and carbon and using a neutralization precipitation method has been proposed (Japanese Unexamined Patent Application Publication No. 1983-1999).
6105, Special Publication Showa 61-26485). The mixtures obtained by these methods are more uniformly mixed than the alumina and carbon mixtures described above, so by firing them in a non-oxidizing atmosphere containing nitrogen, they can be made more uniform and finer than before. Na
It is now possible to obtain AlN powder. However, even in the above improved method, when water or alkali is added dropwise for hydrolysis or neutralization precipitation, precipitates are locally generated and immediately coagulate. For this reason, many aggregates of aluminum hydroxide with a size of 1 μm or more that do not contain fine carbon powder are formed, and the resulting mixture of aluminum hydroxide and carbon has insufficient uniformity. The particle size of the AlN powder obtained by firing such a heterogeneous mixture in a non-oxidizing atmosphere containing nitrogen tends to be irregular, and even after firing, the alumina remains without being nitrided, and the particle size is 1 to 5 μm.
The result was a tendency to form coarse-grained AlN. In order to solve the above problems, the present inventors proposed in Japanese Patent Application No. 61-05863 that they used boehmite (AlOOH) or coagulated boehmite powder, which has excellent dispersibility and stability of the dispersion liquid, and used boehmite (AlOOH) or coagulated boehmite powder to uniformly combine with the carbon source material. We have disclosed a method for obtaining fine AlN powder with a narrow particle size distribution range by preparing a dispersion, solidifying it while maintaining this uniformly dispersed state, drying and firing it. In the above disclosure, when solid carbon is used as a carbon source, the particle size distribution of the obtained AlN powder tends to vary depending on its particle size and dispersion state.
For example, if the particle size exceeds 1 μm, or if the dispersion is insufficient, the particle size may aggregate more than 1 μm.
Many AlN grains were observed, and in extreme cases, nitriding was insufficient and alumina remained. [Problems to be solved by the invention] The present invention provides highly pure and fine particles with excellent sinterability.
The purpose is to further develop the above-mentioned disclosure regarding the method for producing AlN powder, to further improve the quality of the excellent AlN powder, and to provide a method for stably and reproducibly producing fine AlN powder with a narrow particle size distribution range. It is something to do. [Means to solve the problem] AlN with high purity, fine, and excellent sintered body
As a method for producing powder stably and with good reproducibility,
The present invention consists of the following technical means. (1) A boehmite sol in which boehmite is stably dispersed is prepared in advance by adding boehmite or coagulated boehmite powder, which has excellent dispersibility in water, to water and adjusting the pH to a range of 1.2 to 4.5. The boehmite particle size in the boehmite sol is
It is 500 Å or less. Precipitated boehmite has an X-ray diffraction peak at the same position as boehmite crystal, but the peak width is broader than that of boehmite crystal.
Boehmite is poorly crystallized, but it is not much different from boehmite crystals in terms of dispersibility in water. (2) As a carbon source material to be added to the boehmite sol, carbon obtained from a water-soluble organic carbon source material and solid carbon powder are mixed so that the weight ratio of the organic carbon source material and solid carbon powder is in the range of 0.05 to 0.5. A carbon source material blended with is used. This solid carbon powder preferably has a particle size of 0.5 μm or less. After uniformly mixing the total amount of carbon in this carbon source material and boehmite at a weight ratio of 0.4 to 3.0, solidifying while maintaining this uniform mixing state and drying, the mixture is dried in a non-oxidizing atmosphere containing nitrogen. Fire inside. (3) In the step (2) above, in order to maintain the homogeneous mixed state of the boehmite sol and carbon source material dispersion and solidify it, water was removed by evaporation etc. and the boehmite sol was made to coexist with carbon. It is preferable to gel the mixture as it is, then dry it, and then sinter it in a non-oxidizing atmosphere containing nitrogen. Here, the water-soluble organic carbon source material is preferably one that does not affect the dispersibility of the boehmite sol and has a high carbon residual rate at high temperatures, such as a water-soluble resin or lignin sulfonic acid. [Function] The present invention will be specifically explained along with its function. First, boehmite powder or coagulated boehmite powder is added to water, and the pH is adjusted to a range of 1.2 to 4.5 so that the boehmite sol is optimally dispersed. Next, a carbon source material is prepared by blending carbon obtained from a water-soluble organic carbon source material and solid carbon fine powder so that the weight ratio thereof is in the range of 0.05 to 0.5,
The boehmite sol and the carbon source material are uniformly mixed so that the total carbon content in the carbon source material and the boehmite powder are in a weight ratio of 0.4 to 3.0.
This mixture is solidified while maintaining a uniformly mixed state, dried, and then fired at 1350 to 1700°C in a non-oxidizing atmosphere containing nitrogen to obtain AlN powder. The following three methods are used to solidify the above mixture.
A typical example is the street. b) Continue kneading for a long time. Since gelation of the boehmite sol progresses gradually during kneading, the viscosity of the mixture gradually increases and solidifies over time. b) While kneading, water is forcibly volatilized by heating etc. to form a gel state. c) Gelation is promoted by adding acids, alkalis, various ions, polymer flocculants, etc. When making boehmite sol, adjust the pH to 1.2 to 4.5.
The reason for limiting the range is as follows. PH is
If it is less than 1.2, the gelation of the boehmite sol will proceed rapidly, making it virtually impossible to perform the mixing operation with the carbon source material. When the pH exceeds 4.5, boehmite powder is not dispersed in water and remains as an aggregate of 1 μm or more, making it difficult to mix uniformly with the carbon source material. The reason why carbon obtained from a water-soluble organic carbon source material and solid carbon fine powder are blended as the carbon source material so that the weight ratio thereof is in the range of 0.05 to 0.5 is as follows. The effects of the present invention can be maximally achieved by mixing the carbon source material and boehmite sol as uniformly as possible. In order to uniformly mix them, it is first necessary to create a state in which boehmite and carbon are uniformly dispersed. A good dispersion of boehmite can be obtained by adjusting the pH of water as described above. On the other hand, methods for obtaining a good dispersion of a carbon source material include a method of peptizing and dispersing finely powdered solid carbon in a solvent, or a method of dissolving an organic carbon source material in a solvent (in the case of the present invention, the solvent is water). There is a method to use. When only solid carbon powder is used as the carbon source material, the particle size is usually 200 Å even if only fine powder solid carbon is used.
This is the above, and this finely divided carbon is deflocculated to the utmost.
Difficult to disperse. Therefore, an extremely large amount of solid carbon is required to cover the boehmite grains with solid carbon, and the production efficiency of AlN powder becomes extremely low. In addition, if the peptization and dispersion of solid carbon are even slightly insufficient, boehmite may not be reduced and nitrided and may remain as alumina, or the particle size of the resulting AlN powder may become irregular, resulting in poor quality stability and reproducibility. It is also undesirable from a sexual standpoint. In order to solve this problem, it is effective to use a water-soluble organic carbon source material that can easily disperse carbon uniformly. However, if a large amount of organic carbon source material is used, strong bonds between carbons are formed during the high temperature process during AlN powder synthesis, and after the ring element nitridation reaction of boehmite, extremely hard lumps of AlN and carbon are formed. It becomes a thing. That is, in order to treat a mixture of AlN and carbon in an oxidizing atmosphere and decarburize the AlN powder while suppressing oxidation, it is important to crush the above-mentioned lumps as finely as possible in advance. If the lumps are harder than necessary, not only will it take a long time to crush them, but also impurities will inevitably be mixed in during the crushing process.
The residual carbon content also increases. For the above reasons, if the ratio of carbon obtained from the organic carbon source material to solid carbon powder is less than 0.05, the effect of addition is so small that it is virtually unrecognizable, and if this ratio exceeds 0.5, reduction occurs. After the reaction, the lumps of AlN and carbon become extremely hard.
It is regulated between 0.05 and 0.5. The reason why the mixing weight ratio of the total carbon content in the carbon source material to the boehmite powder was limited to a range of 0.4 to 3.0 is as follows. When the weight ratio is less than 0.4, alumina remains even after reductive nitriding, and the particle size also becomes large. If the weight ratio exceeds 3.0, the production efficiency of AIN powder becomes extremely low and is not practical. According to the present invention, fine (1 μm or less) AlN powder with an extremely narrow particle size distribution can be stably produced with good reproducibility. The present invention further improves the prior art in the following two points. (a) By incorporating an appropriate amount of water-soluble organic carbon source material,
The average particle size was smaller and the particle size distribution was narrower, resulting in improved formability and sinterability. (b) AlN that allows carbon to be dispersed in an earlier application
It is extremely sensitive to the properties of the powder and greatly affects it. In contrast, in the present invention, manufacturing variations are small. The AlN powder of the present invention can be easily purified by using high-purity raw material boehmite, for example, the total amount of metal ion impurities can be
It can easily be obtained with a purity of 200 ppm or less. Furthermore, in the present invention, fine boehmite powder and carbon powder are uniformly mixed, so during reductive nitriding,
Impurities such as F 2 O 3 and SiO 2 are easily reduced and volatilized, and as a result, even higher purity AlN powder can be obtained. Further, by using the AlN powder of the present invention, a highly pure and dense sintered body (density of 99% or more) can be easily obtained. [Example] A mixture for producing AlN was prepared using the formulations shown in Table 1, and the mixture was fired at 1450°C for 5 hours in a nitrogen atmosphere, and then decarburized at 650°C for 3 hours.
Got the powder. In Table 1, ... are examples that meet the manufacturing conditions of the present invention, and ... are comparative examples. Mixtures were prepared for all of these using the following procedure. 20% by weight boehmite sol dispersed at PH = 3.0, a dispersant and water were added to solid carbon, and mixed in a pot mill for 10 minutes.
A 15% by weight carbon dispersion obtained by kneading for hours is prepared in advance. After mixing both, a predetermined amount of a water-soluble organic carbon source substance is added. After the addition, the mixture is heated to remove water while stirring, gelatinized, and then dried. The particle size distribution of the above nine types of AlN powders is shown in FIG. 1, and the Al 2 O 3 and carbon contents after the nitriding reaction and after decarburization are shown in Table 2. ~ in Figure 1 and Table 2 correspond to ~ in Table 1, respectively. From Figure 1 and Table 2, we were able to confirm the following. Comparative example, the particle size is coarse and AlBO3 in AlN
The remaining amount is also larger compared to the examples. Furthermore, the particle size distribution and Al 2 O 3 content of the obtained AlN powder tend to vary between production lots. The example is compared to the comparative example.
The particle size is fine, the particle size distribution is narrow, and the variation between lots is small. The amount of Al 2 O 3 remaining after decarburization and the amount of carbon remaining are also small. In the comparative example, since the lumps after the nitriding reaction were too hard, impurities were likely to be mixed in during pulverization. Even when alumina porcelain is used, the Al 2 O 3 content increases due to crushing (Table 2). In addition, the comparative example had a large amount of carbon remaining after decarburization. In the comparative example, a large amount of Al 2 O 3 remains after the nitriding reaction, and the particle size of the AlN powder is also coarse.
【表】【table】
【表】
** アルミナ製粉砕機で粉砕後脱炭したもの。
〔発明の効果〕
本発明によつて高純度で、微細な、均一粒径の
AlN粉を極めて安定的に、再現性よく製造する
ことが可能になつた。
このAlN粉を用いることにより、高密度で、
高熱伝導性、高強度のAlN焼結体を製造するこ
とが容易となり、高温構造材料、IC基板等への
利用に貢献するところが大である。[Table] ** Decarburized after being crushed using an alumina crusher.
[Effects of the Invention] The present invention provides high purity, fine and uniform particle size.
It has become possible to produce AlN powder extremely stably and with good reproducibility. By using this AlN powder, high density,
This makes it easy to produce AlN sintered bodies with high thermal conductivity and high strength, which greatly contributes to their use in high-temperature structural materials, IC substrates, etc.
第1図は種々の方法で合成したAlN粉末の粒
度分布を示すグラフである。
FIG. 1 is a graph showing the particle size distribution of AlN powder synthesized by various methods.
Claims (1)
1.2〜4.5に調整して該ベーマイト粉を分散させた
ベーマイトゾルを作製し、該ベーマイトゾルと炭
素源物質とを混合し、乾燥した後、窒素を含む非
酸化性雰囲気中で焼成する窒化アルミニウム粉末
の製造方法において、有機炭素源物質から得られ
る炭素と固体炭素粉とを重量比で0.05〜0.5の範
囲に配合した炭素源物質を用い、かつ該炭素源物
質中の全炭素量と該ベーマイト粉とを重量比で
0.4〜3.0の割合で混合することを特徴とする窒化
アルミニウム粉末の製造方法。1 Add boehmite powder to a liquid containing water and adjust the pH.
Aluminum nitride powder is produced by preparing a boehmite sol with the boehmite powder adjusted to 1.2 to 4.5, mixing the boehmite sol with a carbon source material, drying, and then firing in a non-oxidizing atmosphere containing nitrogen. In the manufacturing method, a carbon source material containing carbon obtained from an organic carbon source material and solid carbon powder is blended in a weight ratio of 0.05 to 0.5, and the total carbon amount in the carbon source material and the boehmite powder are and in weight ratio
A method for producing aluminum nitride powder, characterized by mixing at a ratio of 0.4 to 3.0.
Priority Applications (6)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62036633A JPS63206306A (en) | 1987-02-19 | 1987-02-19 | Production of aluminum nitride powder |
| KR1019870012944A KR910001300B1 (en) | 1986-11-28 | 1987-11-17 | Process for production of aluminium nitride |
| US07/123,874 US4780299A (en) | 1986-11-28 | 1987-11-23 | Method for producing aluminum nitride powder |
| EP87117496A EP0272493B1 (en) | 1986-11-28 | 1987-11-26 | Method for producing aluminium nitride powder |
| DE8787117496T DE3777116D1 (en) | 1986-11-28 | 1987-11-26 | METHOD FOR PRODUCING ALUMINUM NITRIDE. |
| CA000552817A CA1270365A (en) | 1986-11-28 | 1987-11-26 | Method for producing aluminum nitride powder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62036633A JPS63206306A (en) | 1987-02-19 | 1987-02-19 | Production of aluminum nitride powder |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63206306A JPS63206306A (en) | 1988-08-25 |
| JPH0465003B2 true JPH0465003B2 (en) | 1992-10-16 |
Family
ID=12475240
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62036633A Granted JPS63206306A (en) | 1986-11-28 | 1987-02-19 | Production of aluminum nitride powder |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS63206306A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100788196B1 (en) | 2006-08-24 | 2007-12-26 | 한국과학기술연구원 | Aluminum nitride powder with excellent sinterability and its manufacturing method |
-
1987
- 1987-02-19 JP JP62036633A patent/JPS63206306A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS63206306A (en) | 1988-08-25 |
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