JPS6033204A - Manufacture of powdered bn - Google Patents
Manufacture of powdered bnInfo
- Publication number
- JPS6033204A JPS6033204A JP14186583A JP14186583A JPS6033204A JP S6033204 A JPS6033204 A JP S6033204A JP 14186583 A JP14186583 A JP 14186583A JP 14186583 A JP14186583 A JP 14186583A JP S6033204 A JPS6033204 A JP S6033204A
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- Prior art keywords
- powder
- fluorides
- crystals
- powdered
- oxides
- 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.)
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- Pigments, Carbon Blacks, Or Wood Stains (AREA)
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Abstract
Description
【発明の詳細な説明】
本発明は六方晶BN(以下BNという)粉末の製造法に
関し、特に高充てん性、高結晶性のBN粉末を得ること
を目的とする。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing hexagonal BN (hereinafter referred to as BN) powder, and particularly aims to obtain a BN powder with high filling properties and high crystallinity.
8Nはftfl滑材の外、熱伝導性、電気絶縁性に優れ
、また中性子吸収作用を有するため、樹脂、ゴム、セラ
ミック材等を結合材とする放熱材、中性子遮蔽材のフィ
ラーとしても使用されている。In addition to being used as a ftfl lubricant, 8N has excellent thermal conductivity and electrical insulation, and also has neutron absorption properties, so it is also used as a filler for heat dissipation materials and neutron shielding materials that use resin, rubber, ceramic materials, etc. as binding materials. ing.
これらのフィラーとして重要なことは高充てん性である
こと、さらには結晶性が大なことである。What is important for these fillers is that they have high filling properties and, furthermore, they have great crystallinity.
BNは一般に(よう酸、無水酸化はう素、もしくはほう
砂をアンモニアガス中で加熱するか、或いはこれらほう
酸等に尿素、ジアミン等の加熱分解によりアンモニアガ
スを発生する含窒素有機化合物を混合し、加熱して粗W
BNを得、次いでさらに高温に加熱して再結晶化し、製
品とされている。BN is generally produced by heating ioric acid, anhydrous boronic oxide, or borax in ammonia gas, or by mixing these boric acids with nitrogen-containing organic compounds that generate ammonia gas by thermal decomposition of urea, diamine, etc. , heat and coarsely
BN is obtained and then heated to a higher temperature to recrystallize it to produce a product.
粗製BNは通常100〜1400℃の温度で反応して得
られたもので、結晶が未発達であり、1次結晶の大きさ
は0.1μより小さく、X線回折法で測定されるC軸方
向の結晶化度を示す指数10値も50〜300人と小さ
い(学振炭素材利117委員会法)。Crude BN is usually obtained by reaction at a temperature of 100 to 1400°C, and the crystals are underdeveloped, the size of the primary crystal is smaller than 0.1μ, and the C axis measured by X-ray diffraction method. The index 10 value, which indicates the degree of crystallinity in the direction, is also small, ranging from 50 to 300 (according to JSPS Carbon Materials Research 117 Committee Method).
また、粗製BNは無水酸化はう素からBNに転化する前
駆体としてB−0−N系中間化合物状態で1〜12%の
酸素をBN結晶内に含んでおり、この酸素は未窒化の遊
離の酸化はう素状態の酸素とは異なり、水洗等の常温処
理では除去されないと考えられている。In addition, crude BN contains 1 to 12% of oxygen in the BN crystal in the form of a B-0-N intermediate compound as a precursor for converting anhydrous boron oxide to BN. Unlike oxygen in the boron state, it is thought that the oxidation of
この粗製BNを不活性雰囲気中で粗製B Nの反応住成
温度より高温で再加熱すると、BN結晶中の酸素は遊離
の無水酸化はう素としてBN結晶中より分腑し、Ji散
除去ξれる。再加W4淘度が高くなるとともに酸化はう
素として遊離するMMが多くなり、2000’Cを越え
るとほぼ全mがM離り−る。When this crude BN is reheated in an inert atmosphere at a temperature higher than the reaction temperature of crude BN, the oxygen in the BN crystal is separated from the BN crystal as free anhydrous boron oxide, and Ji dissipation is removed ξ It will be done. As the degree of re-addition W4 increases, the amount of MM liberated as boron oxide increases, and when the temperature exceeds 2000'C, almost all m is separated from M.
これに並行してBNの結晶も発達し、1次結晶の大きさ
は1〜10μになり、LC値は1oooo八を越える。In parallel with this, BN crystals also develop, the size of the primary crystals becomes 1 to 10μ, and the LC value exceeds 1oooo8.
通常市販されているBNは約1900”C以上に加熱さ
れたもので、1次結晶の人込さは1μ以上、LC値は1
000Å以上である。Commercially available BN is heated to about 1900"C or higher, has a primary crystal density of 1μ or more, and has an LC value of 1.
000 Å or more.
このように、結晶の発達したBN粉末を得るためには粗
製BNを不活性気中等で再加熱すればよいが、粗製BN
自体では双粘性に乏しく、再加熱後の粉体の嵩密度は低
く、市販粉末の場合振m嵩密度で0.1〜0,3a/c
cシがなく、樹脂とBN粉体の複合体を得ようとする場
合充てん性が悪く、8Nの特性を発揮するような複合物
が得難い。In this way, in order to obtain BN powder with developed crystals, it is sufficient to reheat crude BN in an inert atmosphere, etc.
By itself, it has poor biviscosity, and the bulk density of the powder after reheating is low, and the bulk density of commercially available powder is 0.1 to 0.3 a/c.
When attempting to obtain a composite of resin and BN powder without C, the filling properties are poor and it is difficult to obtain a composite exhibiting the characteristics of 8N.
従来、充てん性の良′いBN粉体を得る方法としては、
市販のBN粉体に酸化(Jう累、或いは酸化はう素−酸
化カルシウムをバインダーとして加えてホットプレスし
た焼結体を粉砕覆るか、同BN粉末に8203−Ca
O等のほう酸カルシウム塩、或いははうけい酸ガラスを
加えて焼結した焼結体を粉砕する方法があるが、面前の
場合はホットプレス焼結体自体生産性が低く、従って得
られる粉末が高価になる。また、後者の方法では所定組
成のカルシウムはう酸塩、はうけい酸塩が市販品で得難
く、また溶融により自製するには容器との濡れによる融
体の這い上りがあり難しい。Conventionally, the methods for obtaining BN powder with good filling properties are as follows:
Commercially available BN powder is oxidized (J), or boronic oxide-calcium oxide is added as a binder and a hot-pressed sintered body is crushed and covered, or the same BN powder is mixed with 8203-Ca.
There is a method of pulverizing a sintered body that has been sintered by adding calcium borate salt such as O or silicate glass, but in the case of hot press sintering, the productivity of the hot press sintered body itself is low, and the resulting powder is Becomes expensive. In addition, in the latter method, it is difficult to obtain calcium phosphate or silicate with a predetermined composition as a commercially available product, and it is difficult to produce the calcium phosphate or silicate in-house by melting because the molten material creeps up due to wetting with the container.
本発明者は容易に結晶の発達した充てlυ性のよいBN
粉末の製造法を検討した結果、粗製B N l>に存在
する酸素が再加熱で8203になることを利用し、そこ
にアルカリ土類金属の酸化物、或いは弗化物を存在させ
ることにより、これらが焼結バインダーとしてm密化に
効果があり、更に結晶発達にも効果のあることを見出し
、本発明に至ったものである。The present inventors have found that BN with well-developed crystals and good fillability
As a result of studying the method for manufacturing the powder, we found that by utilizing the fact that the oxygen present in crude B N l becomes 8203 when reheated, and by adding an oxide or fluoride of an alkaline earth metal thereto, these The inventors have discovered that, as a sintering binder, they are effective in increasing m-density and are also effective in crystal growth, leading to the present invention.
即ち、本発明はBN結晶中に1〜12%、好ましくは2
〜10%の酸素を含む粗製13N粉末に対し、1〜10
%、好ましくは2〜7%のアルカリ土類金属の酸化物、
或いは弗化物のいずれかの1種、または2種以上の粉末
を添加して圧粉体に成形し、これを不活性ガス等の気流
中、少なくと61700’C以上の温度で焼結させ、粉
砕、分級して結晶の発達した充てん性のよいBN粉末を
4gる方法である。That is, the present invention provides 1 to 12%, preferably 2%, of BN in the BN crystal.
1-10 for crude 13N powder containing ~10% oxygen
%, preferably 2-7% of alkaline earth metal oxides,
Alternatively, one or more powders of fluorides are added and formed into a green compact, and this is sintered at a temperature of at least 61,700'C or higher in a stream of inert gas or the like, This method involves crushing and classifying 4 g of BN powder with developed crystals and good filling properties.
粗製BN中の酸素含有鎖が1%未満ではBN結晶が発達
しすぎて圧粉体の成形が困難となり、また12%を越え
ると加熱時の揮発量が多くなり、焼結体密度が低く、そ
の結果これを粉砕して得られる粉末の嵩密度も低下する
。If the oxygen-containing chains in the crude BN are less than 1%, the BN crystals will develop too much, making it difficult to form a green compact, and if it exceeds 12%, the amount of volatilization during heating will increase, resulting in a low sintered compact density. As a result, the bulk density of the powder obtained by pulverizing it also decreases.
アルカリ土類金属の酸化物、弗化物としては8203と
複塩をつくり、又、BN結晶発達に効果のあるCa O
,Mg0,3a o、Ca F2、MgF2 、Ba
F2が好ましい。Alkaline earth metal oxides and fluorides form double salts with 8203, and CaO is effective for BN crystal development.
, Mg0,3a o, Ca F2, MgF2 , Ba
F2 is preferred.
またこれらの酸化物、弗化物の代りに加熱して酸化物、
弗化物となる炭酸塩、水酸化物、塩基性炭MjM1虐基
性弗化物等を用いてbにい。そのDは酸化物、弗化物換
算でCa記の岳となるようにすればよい。Also, instead of these oxides and fluorides, oxides,
Use carbonates, hydroxides, basic carbons, basic fluorides, etc. to form fluorides. The D may be set to the peak of Ca in terms of oxide and fluoride.
アルカリ土類金属の酸化物もしくは弗化物の添加mは1
%未満か又は10%(内割り%)を越えると焼結性、結
晶性が低く、さらに弗化物の場合は10%を越えると焼
結の除用いるアルミナ質の保護管、ガス吹込み管の損傷
が甚しい。従ってこれらの添加量は1〜10%が適し、
好ましくは2〜7%である。Addition m of alkaline earth metal oxide or fluoride is 1
If it is less than 10% or more than 10% (internal percentage), sinterability and crystallinity will be poor, and in the case of fluoride, if it exceeds 10%, it will be difficult to sinter or use alumina protection tubes or gas blowing tubes. Severe damage. Therefore, the appropriate amount of these additions is 1 to 10%.
Preferably it is 2 to 7%.
BN粉末にこれらの添加物を混合した圧粉体の成形は金
型プレス、ラバープレス等の成形装置を用いて行ない、
その生の高密度が1.3g/cc以上とすることが好ま
しい。この嵩密度が低いと焼結後、粉砕して得られる粉
末の振動充てん高密度が上らない。圧粉体の密度が1.
3g/cc以上であれば、振動充てん高密度として望ま
しい0.6g/cc以上の製品粉末が得られる。 □
圧粉体の加熱はAr1N2ガス等の不活性ガス、NH3
ガス、これらの混合ガス雰囲気下で行なう。A green compact made by mixing these additives with BN powder is formed using a molding device such as a mold press or a rubber press.
It is preferable that the raw high density is 1.3 g/cc or more. If this bulk density is low, the vibration packing density of the powder obtained by pulverization after sintering will not increase. The density of the green compact is 1.
If it is 3 g/cc or more, a product powder of 0.6 g/cc or more, which is desirable as a high-density vibration-filled product, can be obtained. □ Heating the green compact using inert gas such as Ar1N2 gas, NH3
The test is carried out in an atmosphere of gas or a mixture of these gases.
加熱温度は1700℃以上、好ましくは2000〜22
00℃である。1700℃未満で′は結晶の発達が十分
でなく、また2200℃を越えると加熱容器として用い
゛る黒鉛とBNの反応が始まり、84Gの生成があり、
好ましくない。The heating temperature is 1,700°C or higher, preferably 2,000 to 22
It is 00℃. Below 1700°C, the crystals are not sufficiently developed, and above 2200°C, the reaction between graphite used as a heating container and BN begins, producing 84G.
Undesirable.
加熱後、圧粉体は冷却し、ロールミル、ボールミル等の
粉砕機に、より粉砕し、分級する。通常、合成樹脂等の
フィラーとして使用り゛る場合は40メツシユ篩で分級
し、篩下の平均粒径45〜80μnlとなるように粉砕
条件を選ぶことが好ましい。After heating, the green compact is cooled, pulverized in a pulverizer such as a roll mill or a ball mill, and classified. Normally, when used as a filler for synthetic resins, etc., it is preferable to classify with a 40 mesh sieve and select crushing conditions so that the average particle size under the sieve is 45 to 80 μnl.
40メツシユより粗い粒があると樹脂等との複合時表面
が粗くなり、また平均粒径が80μIIIを越えると嵩
密度が低くなり、45μ111より小さいと微粉部分の
吸湿性が影響して流動性も低下してくる。If there are particles coarser than 40 mesh, the surface will be rough when combined with resin, etc. If the average particle size exceeds 80μIII, the bulk density will be low, and if it is smaller than 45μ111, the hygroscopicity of the fine powder will affect the fluidity. It's going to decline.
本発明のBN粉末は充てん性、結晶性が良いので、樹脂
、シリコーンゴムとの複合体において、多量にBNを含
有せしめることができ、例えば放熱シートであれば、熱
放散性が良好となる。Since the BN powder of the present invention has good filling properties and crystallinity, a large amount of BN can be contained in a composite with a resin or silicone rubber. For example, if it is a heat dissipation sheet, the heat dissipation property will be good.
実施例1〜4
はう酸を燐酸カルシウム(フィラー)と混合、粉砕し、
造粒及び乾燥後アンモニアガス中で850℃に加熱、窒
化し、常法によりフィラー及び未反応物を除去し粗製B
Nを得た。この粗製BN中の酸素量は10%であった。Examples 1 to 4 Mixing and pulverizing oxalic acid with calcium phosphate (filler),
After granulation and drying, it was heated to 850°C in ammonia gas, nitrided, and the filler and unreacted substances were removed by a conventional method to obtain crude B.
I got N. The amount of oxygen in this crude BN was 10%.
この粗製BNに対し、それぞれ炭酸カルシウム、炭酸マ
グネシウム、炭酸バリウム、弗化カルシウムを添加混合
した。添加量は酸化物、及び弗化物の状態で11製13
Nに対し5%とした。これを1500kg/ Cm2
の加圧力で60耐の円柱状に成形し高密)哀1.37〜
−1.47g/ccの圧粉体を得た。この圧粉体を黒鉛
ルツボに入れ、高周波加熱炉に挿入し、ルツボ内に窒素
ガスをI Q/+11in、流しながら2Hrで200
0〜2100℃に昇温、この温度に21−1 r保持し
た。窒素ガスを流しながら冷却し、黒鉛ルツボよりBN
圧粉体を取り加物の場合にも、高高密度の粉末であった
。Calcium carbonate, magnesium carbonate, barium carbonate, and calcium fluoride were added and mixed to this crude BN, respectively. The amount added is 11 and 13 in the form of oxides and fluorides.
It was set to 5% with respect to N. This is 1500kg/cm2
Formed into a cylindrical shape with a resistance of 60 with a pressure of 1.37~
A green compact of -1.47 g/cc was obtained. This green compact was placed in a graphite crucible, inserted into a high-frequency heating furnace, and heated for 200 hours for 2 hours while flowing nitrogen gas at IQ/+11 inches into the crucible.
The temperature was raised to 0 to 2100°C and maintained at this temperature for 21-1 r. Cool while flowing nitrogen gas, and transfer to BN from a graphite crucible.
Even when the green compact was used as a filler, it was a high-density powder.
比較例1
上記実施例と同様にして得た粗製13 Nを実施例と同
じ条件で60 m nlφの圧粉体とし、窒素ガスを流
しながら加熱、冷却、粉砕、分級した。(9られたBN
粉末の振動高密度1ユ表1に示す如く、0.55g/c
cであった。Comparative Example 1 Crude 13N obtained in the same manner as in the above example was made into a compact of 60 m nlφ under the same conditions as in the example, and heated, cooled, pulverized, and classified while flowing nitrogen gas. (9 BN
Powder vibration high density 1U As shown in Table 1, 0.55g/c
It was c.
実施例5〜8
乾燥朋水はう砂と尿素を混合し、アンモニアガス中で1
000℃まで加熱窒化し、常法により未反応物を除−去
しC粗製BN粉末を得た。この粗製BN粉末中の酸素量
は3%であった。Examples 5 to 8 Dry Hosui sand and urea were mixed and mixed in ammonia gas for 1
The mixture was nitrided by heating to 000° C., and unreacted substances were removed by a conventional method to obtain C crude BN powder. The amount of oxygen in this crude BN powder was 3%.
この粗製BN粉末にそれぞれCa O,MgO。CaO and MgO were added to this crude BN powder, respectively.
MgF2.3a F2を添加混合し、実施例1〜4と同
様に圧粉体形状で加熱後、粉砕、分級して表1に示す如
き嵩密度のBN粉末を得た。MgF2.3a F2 was added and mixed, heated in the form of a green compact in the same manner as in Examples 1 to 4, and then crushed and classified to obtain BN powder having a bulk density as shown in Table 1.
比較例2
上記実施例5〜8と同様にして得た粗製BNに添加物を
添加せずに上記と同じ条件で処理し、BN粉末を得た。Comparative Example 2 Crude BN obtained in the same manner as in Examples 5 to 8 above was treated under the same conditions as above without adding any additives to obtain BN powder.
実施例5〜8で得たBN粉末は比較例2で得たものに比
べ、焼結効果があり、振動高密度も高くなっている。The BN powders obtained in Examples 5 to 8 have a sintering effect and a higher vibration density than those obtained in Comparative Example 2.
比較例3
実施例5〜8ど同様にして得た粗製BN粉末を1400
℃に再加熱し、水洗、乾燥により、酸素含有ff! 0
.5%の粗製[3N粉末を得た。この低酸素粗製PNI
介生じつい12%(、+n相嘉の岸醋カルシウムを加え
て前記各実施例と同様に焼成、粉砕、分級を行なったが
、この場合には成形が困難で、圧粉体の高密度が低いた
め焼結後の粉末のm密度も実施例に比べ低下していた。Comparative Example 3 Crude BN powder obtained in the same manner as Examples 5 to 8 was
By reheating to ℃, washing with water, and drying, the oxygen-containing ff! 0
.. 5% crude [3N powder was obtained. This hypoxic crude PNI
Calcination, pulverization, and classification were performed in the same manner as in the above examples with the addition of 12% (+n) Aika's Kishimi calcium, but in this case, molding was difficult and the high density of the green compact Because of the low density, the m-density of the powder after sintering was also lower than that of the example.
(以下余白)(Margin below)
Claims (1)
リ土類金属の酸化物、弗化物、もしくは加熱により酸化
物、弗化物となる化合物から選ばれた少なくとも1種の
粉末を酸化物、弗化物換算で1〜10重量%混合、成形
し、不活性ガスもしくはNH3気流中、1700℃以上
で焼結し、この焼結体を粉砕、分級することを特徴とす
るBN粉末の製造法。At least one powder selected from alkaline earth metal oxides, fluorides, or compounds that become oxides or fluorides upon heating is added to undeveloped BN powder containing 1 to 12% by weight of oxygen. A method for producing BN powder, which comprises mixing 1 to 10% by weight in terms of compounds, molding, sintering at 1700°C or higher in an inert gas or NH3 stream, and pulverizing and classifying the sintered body.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14186583A JPS6033204A (en) | 1983-08-04 | 1983-08-04 | Manufacture of powdered bn |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14186583A JPS6033204A (en) | 1983-08-04 | 1983-08-04 | Manufacture of powdered bn |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6033204A true JPS6033204A (en) | 1985-02-20 |
| JPS6227002B2 JPS6227002B2 (en) | 1987-06-11 |
Family
ID=15301959
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP14186583A Granted JPS6033204A (en) | 1983-08-04 | 1983-08-04 | Manufacture of powdered bn |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6033204A (en) |
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0174452U (en) * | 1987-10-30 | 1989-05-19 | ||
| JP2001508019A (en) * | 1997-11-12 | 2001-06-19 | ローベルト ボツシユ ゲゼルシヤフト ミツト ベシユレンクテル ハフツング | Boron nitride packing compact |
| WO2011043082A1 (en) * | 2009-10-09 | 2011-04-14 | 水島合金鉄株式会社 | Hexagonal boron nitride powder and method for producing same |
| WO2016092951A1 (en) * | 2014-12-08 | 2016-06-16 | 昭和電工株式会社 | Hexagonal boron nitride powder, method for producing same, resin composition, and resin sheet |
| WO2016092952A1 (en) * | 2014-12-08 | 2016-06-16 | 昭和電工株式会社 | Hexagonal boron nitride powder, method for producing same, resin composition, and resin sheet |
| JP2021102536A (en) * | 2019-12-25 | 2021-07-15 | デンカ株式会社 | Hexagonal boron nitride powder, method for producing the same, cosmetic and method for evaluating quality |
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-
1983
- 1983-08-04 JP JP14186583A patent/JPS6033204A/en active Granted
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| JPH0174452U (en) * | 1987-10-30 | 1989-05-19 | ||
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Also Published As
| Publication number | Publication date |
|---|---|
| JPS6227002B2 (en) | 1987-06-11 |
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