JPH0226813A - Purification of aluminum nitride powder - Google Patents
Purification of aluminum nitride powderInfo
- Publication number
- JPH0226813A JPH0226813A JP17258488A JP17258488A JPH0226813A JP H0226813 A JPH0226813 A JP H0226813A JP 17258488 A JP17258488 A JP 17258488A JP 17258488 A JP17258488 A JP 17258488A JP H0226813 A JPH0226813 A JP H0226813A
- Authority
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- Japan
- Prior art keywords
- aluminum nitride
- powder
- nitride powder
- oxygen content
- carbon
- Prior art date
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Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は、新規な窒化アルミニウム粉末の精製方法に関
するものである。DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a novel method for purifying aluminum nitride powder.
(従来の技術)
窒化アルミニウム粉末(^ff1N)は理論的には30
0W/m、に以上と酸化ベリラム(Bed)に匹敵する
高い熱伝導率を有し、絶縁性、誘電性などの電気的性質
にもすぐれることから、大電力化や高集積化が進む半導
体用絶縁放熱基板材料として非常に注目されている。(Prior art) Aluminum nitride powder (^ff1N) is theoretically 30
It has a high thermal conductivity of more than 0 W/m, comparable to beryllum oxide (Bed), and has excellent electrical properties such as insulation and dielectricity, making it a semiconductor that is becoming more powerful and highly integrated. It is attracting a lot of attention as an insulating heat dissipation substrate material.
ところで、理論的には高い熱伝導率を有するAfNであ
るが、得られた焼結体の熱伝導率を左右する大きな要因
のひとつは、エレクトロセラミクス(Vol、17 1
1月号(1986)P、33〜P、40)に示される様
にAfN粉末原料中の酸素不純物量である。Incidentally, although AfN theoretically has a high thermal conductivity, one of the major factors that influences the thermal conductivity of the obtained sintered body is electroceramics (Vol. 17 1).
As shown in January issue (1986) P, 33-P, 40), this is the amount of oxygen impurities in the AfN powder raw material.
従来、AZN粉末中の酸素含有量を低減させるためには
、へlN生成反応を充分行なわせることでその解決を計
ろうとしてきたが、それでもAffiN粉末中の酸素含
有量はAl2N粉末の合成方法によって異なるが約1重
量%前後もしくはそれより多かった。Conventionally, attempts have been made to reduce the oxygen content in AZN powder by sufficiently carrying out the HelN production reaction, but the oxygen content in AffiN powder still varies depending on the synthesis method of Al2N powder. Although it varies, it was around 1% by weight or more.
Al2N粉末を処理して酸素含有量を低減させる方法と
しては、特開昭60−71576号にAINと遊離炭素
、炭素含有有機物質およびそれらの混合物等の炭素質添
加剤とから成る粒状混合物をアルゴン、窒素およびそれ
らの混合物から選ばれた非酸化性雰囲気中で加熱処理す
る方法が示されている。この方法によれば、AfN粉末
と炭素質添加剤とから成る粒状混合物を形成しなければ
ならず、炭素質添加剤の正確な添加が必要であり、多く
添加すれば加熱処理後残留炭素量が増加する。As a method for treating Al2N powder to reduce the oxygen content, Japanese Patent Application Laid-open No. 71576/1983 describes a method in which a granular mixture of AIN and carbonaceous additives such as free carbon, carbon-containing organic substances, and mixtures thereof is heated with argon. , nitrogen, and mixtures thereof. According to this method, a granular mixture consisting of AfN powder and carbonaceous additive must be formed, and the carbonaceous additive must be added accurately, and if a large amount is added, the amount of residual carbon after heat treatment will be reduced. To increase.
(本発明が解決しようとする問題点)
本発明が解決しようとする点は、酸素含有量の少ないA
IN粉末を得るためのIN粉末の精製方法を提供するに
ある。(Problems to be solved by the present invention) The problems to be solved by the present invention are
The present invention provides a method for purifying IN powder to obtain IN powder.
(問題を解決するための手段)
本発明者らは上記の問題点について鋭意研究を行った結
果、酸素含有量の少ないAj2N粉末を容易に得るAf
fiN粉末の精製方法を見い出した。(Means for Solving the Problem) As a result of intensive research into the above-mentioned problems, the present inventors found that Af
We have discovered a method for purifying fiN powder.
すなわち、本発明はAfN粉末をカーボン製容器に収容
し、窒素もしくは窒素を含む不活性ガス中で1200〜
1800°Cで加熱処理することを特徴とするAfN粉
末精製方法である。That is, in the present invention, AfN powder is stored in a carbon container and heated to 1200 to
This is an AfN powder purification method characterized by heat treatment at 1800°C.
さらに詳しくは、本発明に用いるAi!、N粉末につい
て、平均粒径、酸素含有量、比表面積について特に限定
されないが、平均粒径については、走査型電子顕微鏡観
察によって求まる平均粒径が0.05〜lumのものが
適しており、さらには0.1〜0.8μm、さらには0
.2〜0.6μmのものが好ましい。また遠心沈降法に
よって求まる平均粒径は0.5〜3μmのものが適して
おり、さらには0.5〜1.5μmさらには0.6〜1
.0μmのものが好ましい。酸素含有量については、0
.7〜3.0重量、さらには0.8〜2.0重量%、ま
たさらには0.8〜1.5重量%のものが好ましい。More specifically, Ai! used in the present invention! Regarding the N powder, there are no particular limitations on the average particle size, oxygen content, and specific surface area, but it is suitable that the average particle size determined by scanning electron microscopy is 0.05 to lum. Furthermore, 0.1 to 0.8 μm, and even 0
.. A thickness of 2 to 0.6 μm is preferable. In addition, the average particle size determined by centrifugal sedimentation is preferably 0.5 to 3 μm, more preferably 0.5 to 1.5 μm, and even 0.6 to 1 μm.
.. Preferably, the thickness is 0 μm. For oxygen content, 0
.. 7 to 3.0% by weight, more preferably 0.8 to 2.0% by weight, and even more preferably 0.8 to 1.5% by weight.
比表面積については、1ryf/g以上が好ましく、さ
らには2rrf/g以上、またさらには3rrf/g以
上のものが好ましい。The specific surface area is preferably 1 ryf/g or more, more preferably 2 rrf/g or more, and even more preferably 3 rrf/g or more.
上記のAfN粉末をカーボン製の容器に収容し、加熱処
理するが用いるカーボン製の容器はできるだけ高純度の
ものが望ましいがもし低純度のものであれば、塩素ガス
中で加熱処理を行なった後使用するのが望ましい。カー
ボン製容器の形状は特には限定されない。The above AfN powder is placed in a carbon container and heat-treated. It is desirable that the carbon container used be as pure as possible, but if it is of low purity, it should be heat-treated in chlorine gas. It is preferable to use The shape of the carbon container is not particularly limited.
AffN粉末をカーボン製の容器に収容したのち加熱処
理するが、その雰囲気は、窒素もしくは窒素を含む不活
性ガス中である。この場合、不活性ガスとはヘリウム、
ネオン、アルゴンをさす。加熱温度は1200〜180
0°Cであり、好ましくは1300〜1600°C1さ
らに好ましくは1350〜1550°Cである。The AffN powder is placed in a carbon container and then heat-treated in an atmosphere of nitrogen or an inert gas containing nitrogen. In this case, the inert gas is helium,
Neon and argon. Heating temperature is 1200-180
0°C, preferably 1300 to 1600°C, more preferably 1350 to 1550°C.
特許請求の範囲を越える温度では、酸素含有量の低減は
認められるが、粒子同志の焼結が進み、大きな凝集を形
成し始めるため好ましくない。また、特許請求の範囲を
下回る温度では、酸素含有量の低減効果が小さく好まし
くない。ガス流量は、加熱処理するAfN粉末の量、あ
るいは加熱処理に用いる炉の構造によりても異なるので
特に限定されないが、できれば、流量の多い方が酸素低
減は行ないやすい。At temperatures exceeding the claimed range, although a reduction in oxygen content is observed, sintering of the particles progresses and large agglomerates begin to form, which is not preferable. Further, at a temperature lower than the claimed range, the effect of reducing oxygen content is small, which is not preferable. The gas flow rate is not particularly limited as it varies depending on the amount of AfN powder to be heat treated or the structure of the furnace used for the heat treatment, but if possible, oxygen reduction will be easier if the flow rate is large.
また、AfN粉末のカーボン製容器への収容状態である
が、あまり密に充填した場合、酸素含有量の低減が行な
いにくい場合もあり、充填密度としては、0.05〜0
.8g/ccが望ましく、さらには、0.10〜0.6
0g/cc、またさらには0.15〜0.50g/cc
が望ましい。In addition, regarding the state in which AfN powder is stored in a carbon container, if it is packed too densely, it may be difficult to reduce the oxygen content, so the packing density is 0.05 to 0.
.. 8 g/cc is desirable, and more preferably 0.10 to 0.6
0g/cc, or even 0.15-0.50g/cc
is desirable.
本発明によって得られるIN粉末の酸素含有量は、未処
理のAj2N粉末の酸素含有量の273から1/6程度
に低減されたものになるが通常は1/2から1/4程度
が行ないやすい。The oxygen content of the IN powder obtained by the present invention is reduced to about 1/6 from 273 of the oxygen content of untreated Aj2N powder, but it is usually easier to reduce the oxygen content to about 1/2 to 1/4. .
本発明によって処理されて得られたAj2N粉末に適当
な焼結助剤を添加し焼結させて得られたAI!、N焼結
体は、未処理のIRON粉末から得られたAj2N焼結
体に比較して高い熱伝導率を示す。AI obtained by adding a suitable sintering aid to the Aj2N powder obtained by the treatment according to the present invention and sintering it! , N sintered bodies exhibit higher thermal conductivity compared to Aj2N sintered bodies obtained from untreated IRON powder.
次に本発明における実施例について以下の様に行った。 Next, an example of the present invention was carried out as follows.
実施例に記載の^2N粉末の遠心沈降法による平均粒径
は、セイシン企業社製粒度分布ミクロフォトサイザー5
KA−5000を用い、溶媒にイソブチルアルコールを
用いて遠心沈降法により測定し、50重量%径を平均粒
径とした。The average particle size determined by the centrifugal sedimentation method of the ^2N powder described in the Examples was determined using Particle Size Distribution Micro Photosizer 5 manufactured by Seishin Enterprise Co., Ltd.
The particles were measured by centrifugal sedimentation using KA-5000 and isobutyl alcohol as a solvent, and the 50% by weight diameter was defined as the average particle diameter.
SEM (走査型電子顕微鏡)観察は、日立製作所型の
S−650型走査型電子顕微鏡により行った。SEM (scanning electron microscope) observation was performed using a Hitachi S-650 scanning electron microscope.
SEM観察によって求める平均粒径Xは単位視野内に見
えるn個の粒子の粒径Xiを測定し次式より算出したも
のをいう。The average particle diameter X determined by SEM observation is calculated from the following formula by measuring the particle diameters Xi of n particles visible within a unit field of view.
本発明では約300個の粒子についてその粒径を測定し
て平均粒径を求めた。In the present invention, the average particle size was determined by measuring the particle size of about 300 particles.
AIN粉末の比表面積は窒素ガスの吸着によるBET法
により求めた。The specific surface area of the AIN powder was determined by the BET method using nitrogen gas adsorption.
AffiN粉末中の酸素含有量はLECO社製TC−1
36型分析装置により行った。The oxygen content in AffiN powder is TC-1 manufactured by LECO.
The analysis was carried out using a Model 36 analyzer.
AfN粉末中の金属不純物の分析は、日本ジャーレル・
アッシュ■製の発光分光分析装置ICAP−575Ma
rkI[で行った。Analysis of metal impurities in AfN powder is conducted by Nippon Jarrell Co., Ltd.
Emission spectrometer ICAP-575Ma manufactured by Ash ■
I went with rkI [.
またAIN焼結体の熱伝導率は、真空理工社製レーザフ
ラッシュ法熱定数測定装置TC−3000型により測定
した。The thermal conductivity of the AIN sintered body was measured using a laser flash method thermal constant measuring device TC-3000 manufactured by Shinku Riko Co., Ltd.
実施例1
遠心沈降法による平均粒径が1.5μm 、 58M観
察により求めた平均粒径が0.56μm、比表面積が3
.6 rrf/g、酸素含有量が0.95重量%で、金
属不純物量が0.03重量%であるAlN粉末を内径1
00 mmのカーボンルツボに充填した。そのカーボン
ルツボを電気炉に入れ窒素ガス流量を542 /min
として表1に示す条件下で処理した。結果を表1に示す
。Example 1 Average particle size determined by centrifugal sedimentation method is 1.5 μm, average particle size determined by 58M observation is 0.56 μm, and specific surface area is 3
.. 6 rrf/g, an oxygen content of 0.95% by weight, and an amount of metal impurities of 0.03% by weight.
00 mm carbon crucible. Place the carbon crucible in an electric furnace and set the nitrogen gas flow rate to 542/min.
The samples were treated under the conditions shown in Table 1. The results are shown in Table 1.
実施例2
遠心沈降法による平均粒径が0.87μs 、 58M
観察により求めた平均粒径が0.28μm、比表面積が
6.9 rd/g、酸素含有量が1.21重量%で、金
属不純物量が0.08重量%であるA2N粉末を内径1
00 mのカーボンルツボに充填し、そのカーボンルツ
ボを電気炉に入れ窒素ガス流量を51 /minとして
表1に示す条件下で処理した。結果を表1に示す。Example 2 Average particle size by centrifugal sedimentation method is 0.87 μs, 58M
An A2N powder with an average particle diameter of 0.28 μm, a specific surface area of 6.9 rd/g, an oxygen content of 1.21% by weight, and a metal impurity content of 0.08% by weight, determined by observation, was prepared with an inner diameter of 1
The carbon crucible was filled in a carbon crucible with a diameter of 0.00 m, and the carbon crucible was placed in an electric furnace and treated under the conditions shown in Table 1 with a nitrogen gas flow rate of 51/min. The results are shown in Table 1.
実施例3
遠心沈降法による平均粒径が0.80tIm 、 58
M観察により求めた平均粒径が0.15μm、酸素含有
量が2.30重量%、金属不純物量が0.05重景%の
Aj2N粉末を内径100 mmのカーボンルツボに充
填し、そのカーボンルツボを電気炉に入れ窒素ガスを1
027m1nとして、表1に示す条件下で処理した。結
果を表1に示す。Example 3 Average particle size by centrifugal sedimentation method is 0.80 tIm, 58
Aj2N powder with an average particle size of 0.15 μm determined by M observation, an oxygen content of 2.30% by weight, and a metal impurity amount of 0.05% by weight was filled into a carbon crucible with an inner diameter of 100 mm, and the carbon crucible was into an electric furnace and add 1 liter of nitrogen gas.
027mln and processed under the conditions shown in Table 1. The results are shown in Table 1.
比較例
実施例1で用いたAfN粉末を表1に示す処理条件以外
は、全〈実施例1と同様に行った。その結果を表1に示
す。Comparative Example The AfN powder used in Example 1 was treated in the same manner as in Example 1 except for the treatment conditions shown in Table 1. The results are shown in Table 1.
(以下余白)
表 1
(発明の効果)
以上説明したように本発明の窒化アルミニウム粉末の精
製方法は、A1N粉末の酸素含有量を簡単に低減できる
方法である。この方法によって酸素含有量が低減された
AlN粉末は、従来のAI!、N粉末に比較して、焼結
助剤の添加量が少なくでき、かつ得られた焼結体は高い
熱伝導率を示す。(The following is a blank space) Table 1 (Effects of the Invention) As explained above, the method for refining aluminum nitride powder of the present invention is a method that can easily reduce the oxygen content of A1N powder. AlN powder whose oxygen content has been reduced by this method is similar to conventional AI! , compared to N powder, the amount of sintering aid added can be reduced, and the obtained sintered body exhibits high thermal conductivity.
したがって本発明は、今後、熱特性が非常に強く要求さ
れる大規模集積回路基板をはじめとした幅広い電子材料
への用途に用いられる^fN焼結体の原料粉末の精製方
法として有効である。Therefore, the present invention is effective as a method for purifying raw material powder for ^fN sintered bodies that will be used in a wide range of electronic materials including large-scale integrated circuit boards that will require very strong thermal properties.
特許出願人 旭化成工業株式会社Patent applicant: Asahi Kasei Industries, Ltd.
Claims (1)
素もしくは窒素を含む不活性ガス中で1200〜180
0℃で加熱処理することを特徴とする窒化アルミニウム
粉末の精製方法Aluminum nitride powder is stored in a carbon container and heated to 1200 to 180 in nitrogen or an inert gas containing nitrogen.
A method for refining aluminum nitride powder, characterized by heat treatment at 0°C
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP17258488A JPH0226813A (en) | 1988-07-13 | 1988-07-13 | Purification of aluminum nitride powder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP17258488A JPH0226813A (en) | 1988-07-13 | 1988-07-13 | Purification of aluminum nitride powder |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0226813A true JPH0226813A (en) | 1990-01-29 |
Family
ID=15944551
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP17258488A Pending JPH0226813A (en) | 1988-07-13 | 1988-07-13 | Purification of aluminum nitride powder |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0226813A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5866670A (en) * | 1995-08-21 | 1999-02-02 | Polyplastics Co., Ltd. | Process for preparing polyacetal copolymer |
| JP2007315981A (en) * | 2006-05-29 | 2007-12-06 | Hioki Ee Corp | Measuring device and inspection device |
-
1988
- 1988-07-13 JP JP17258488A patent/JPH0226813A/en active Pending
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5866670A (en) * | 1995-08-21 | 1999-02-02 | Polyplastics Co., Ltd. | Process for preparing polyacetal copolymer |
| JP2007315981A (en) * | 2006-05-29 | 2007-12-06 | Hioki Ee Corp | Measuring device and inspection device |
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