JP2522981B2 - Method for producing fibrous magnesium pyroborate - Google Patents

Method for producing fibrous magnesium pyroborate

Info

Publication number
JP2522981B2
JP2522981B2 JP63041726A JP4172688A JP2522981B2 JP 2522981 B2 JP2522981 B2 JP 2522981B2 JP 63041726 A JP63041726 A JP 63041726A JP 4172688 A JP4172688 A JP 4172688A JP 2522981 B2 JP2522981 B2 JP 2522981B2
Authority
JP
Japan
Prior art keywords
magnesium
pyroborate
source compound
raw material
fibrous magnesium
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 - Lifetime
Application number
JP63041726A
Other languages
Japanese (ja)
Other versions
JPH01215709A (en
Inventor
幸治 坂根
孝雄 北村
淳 小川
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Otsuka Chemical Co Ltd
National Institute of Advanced Industrial Science and Technology AIST
Original Assignee
Agency of Industrial Science and Technology
Otsuka Chemical Co Ltd
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Description

【発明の詳細な説明】 産業上の利用分野 本発明は、繊維状ピロホウ酸マグネシウムの製造方法
に関する。繊維状ピロホウ酸マグネシウムは、プラスチ
ック、金属、セラミックス、コンクリート等の複合強化
材、摩擦材料、過材料、バッテリーの隔膜、顔料、絶
縁材料、耐熱性材料等として有用である。
TECHNICAL FIELD The present invention relates to a method for producing fibrous magnesium pyroborate. Fibrous magnesium pyroborate is useful as a composite reinforcing material such as plastic, metal, ceramics, concrete, friction material, excess material, battery diaphragm, pigment, insulating material, and heat resistant material.

従来の技術及びその問題点 従来、繊維状ピロホウ酸マグネシウムは、マグネシウ
ム源化合物、ホウ素源化合物及びフラックスをミキサー
等を用いた機械的方法により乾式混合し、この混合物を
加熱処理して製造されている(例えば特開昭60−204697
号公報参照)。
Conventional technology and its problems Conventionally, fibrous magnesium pyroborate is produced by dry-mixing a magnesium source compound, a boron source compound and a flux by a mechanical method using a mixer or the like, and heat-treating this mixture. (For example, JP-A-60-204697
(See the official gazette).

しかしながら、この方法に従えば、繊維状ピロホウ酸
マグネシウムは、大部分の繊維が塊状に固まった集合塊
(ショット)として生成するを避け得ない。而して斯か
るショットを構成している繊維を解繊する操作において
は、繊維が折損、粉砕されるために、繊維長が短くなっ
たり、繊維の品質及び繊維収率が低下したりする等の問
題が生ずる。
However, according to this method, most of the fibrous magnesium pyroborate is inevitably formed as an aggregated mass (shot) in which most of the fibers are solidified into a mass. Thus, in the operation of defibrating the fibers constituting such a shot, the fibers are broken or crushed, so that the fiber length is shortened, the quality of the fibers and the fiber yield are decreased, etc. The problem of occurs.

問題点を解決するための手段 本発明の目的は、ショットがなく、解繊し易く且つ長
さや太さの揃った品質の良好な繊維状ピロホウ酸マグネ
シウムの製造方法を提供することにある。
Means for Solving the Problems An object of the present invention is to provide a method for producing fibrous magnesium pyroborate, which has no shots, is easy to be defibrated, and has a uniform length and thickness, and is of good quality.

本発明の目的は、繊維状ピロホウ酸マグネシウムを製
造するに当り、マグネシウム源化合物、ホウ素源化合物
及びフラックスを含有し且つマグネシウム源化合物を微
粒化して原料混合物中に均一に分散させた原料混合溶液
を噴霧乾燥し、次いで得られる噴霧乾燥物を約10℃/分
以下の速度で850℃前後まで昇温し、この温度で処理す
ることにより達成される。
The object of the present invention is to produce a fibrous magnesium pyroborate, a raw material mixed solution containing a magnesium source compound, a boron source compound and a flux and atomizing the magnesium source compound to uniformly disperse the raw material mixed solution in the raw material mixture. It is achieved by spray-drying, then raising the temperature of the resulting spray-dried product to about 850 ° C. at a rate of about 10 ° C./minute or less, and treating at this temperature.

本発明で用いられるマグネシウム源化合物としては、
従来公知のものを広く使用でき、マグネシウムの酸化
物、水酸化物の他、無機酸、炭酸、硫酸、硝酸、ハロゲ
ン化水素酸のマグネシウム塩のようなマグネシウム化合
物が挙げられる。このような化合物としては、具体的に
は酸化マグネシウム、水酸化マグネシウム、塩基性炭酸
マグネシウム、硫酸マグネシウム、塩化マグネシウム、
臭化マグネシウム等を例示できる。これらは単独で用い
てもよいし、2種以上混合して用いてもよい。
As the magnesium source compound used in the present invention,
Conventionally known compounds can be widely used, and in addition to magnesium oxide and hydroxide, magnesium compounds such as inorganic acid, carbonic acid, sulfuric acid, nitric acid, and magnesium salt of hydrohalic acid can be mentioned. As such a compound, specifically, magnesium oxide, magnesium hydroxide, basic magnesium carbonate, magnesium sulfate, magnesium chloride,
Examples include magnesium bromide and the like. These may be used alone or in combination of two or more.

本発明で用いられるホウ素源化合物としても、従来公
知のものを広く使用でき、例えば酸化ホウ素等のホウ素
の酸化物、オルトホウ酸(H3BO3)、四ホウ酸(H2B
4O7)、メタホウ酸(HBO2)等のホウ素の酸素酸、又は
これらのアルカリ金属塩(例えばホウ酸ナトリウム、ピ
ロホウ酸ナトリウム、ピロホウ酸カリウム、メタホウ酸
ナトリウム等)等が挙げられる。これらは単独で用いて
もよいし、2種以上混合して用いてもよい。
As the boron source compound used in the present invention, conventionally known compounds can be widely used, and examples thereof include boron oxides such as boron oxide, orthoboric acid (H 3 BO 3 ), tetraboric acid (H 2 B 2
4 O 7 ), oxyboric acid such as metaboric acid (HBO 2 ), or alkali metal salts thereof (for example, sodium borate, sodium pyroborate, potassium pyroborate, sodium metaborate, etc.) and the like. These may be used alone or in combination of two or more.

また本発明で用いられるフラックスとしては、例えば
塩化カリウム、塩化ナトリウム等を挙げることができ、
これらは1種単独で又は混合して使用される。
Examples of the flux used in the present invention include potassium chloride and sodium chloride,
These may be used alone or in combination.

上記マグネシウム源化合物、ホウ素源化合物及びフラ
ックスの配合割合としては、特に限定されるものではな
いが、通常マグネシウム源化合物とホウ素源化合物のモ
ル比が1:4から1:1であり且つフラックスが全重量に基づ
き10〜95重量%となるように3者を配合するのがよい。
本発明では、特にマグネシウム源化合物、ホウ素源化合
物及びフラックスを2:3:7(モル比)の割合で配合する
のが好適である。
The mixing ratio of the magnesium source compound, the boron source compound and the flux is not particularly limited, but usually the molar ratio of the magnesium source compound and the boron source compound is 1: 4 to 1: 1 and the total flux. It is advisable to mix the three components so that the amount is 10 to 95% by weight based on the weight.
In the present invention, it is particularly preferable to mix the magnesium source compound, the boron source compound and the flux at a ratio of 2: 3: 7 (molar ratio).

本発明では、上記マグネシウム源化合物を微粒化して
原料混合物中に均一に分散させておくことが必要であ
る。マグネシウム源化合物の微粒化・均一分散化の方法
としては、例えば下記A、Bの方法を挙げることができ
る。
In the present invention, it is necessary to atomize the magnesium source compound and uniformly disperse it in the raw material mixture. Examples of the method for atomizing and uniformly dispersing the magnesium source compound include the following methods A and B.

方法A: 不溶性のマグネシウム源化合物を酸又はアルカリの作
用により可溶化し、これを水に溶解して水溶液としたも
の、或は可溶性のマグネシウム源化合物(例えば可溶性
マグネシウム塩)を水に溶解して水溶液としたものに、
アルカリ又は酸を加えて中和すると、コロイド状の不溶
性マグネシウム源化合物を懸濁液の形態で得ることがで
きる。該コロイド状不溶性マグネシウム源化合物の懸濁
液に、ホウ素源化合物及びフラックスを添加し、混合す
ると、マグネシウム源化合物が微粒化、均一分散化され
た原料混合物を得ることができる。
Method A: An insoluble magnesium source compound is solubilized by the action of an acid or an alkali and dissolved in water to give an aqueous solution, or a soluble magnesium source compound (for example, a soluble magnesium salt) is dissolved in water. To what was made into an aqueous solution,
Upon addition of an alkali or acid to neutralize, the colloidal insoluble magnesium source compound can be obtained in the form of a suspension. When the boron source compound and the flux are added to and mixed with the suspension of the colloidal insoluble magnesium source compound, a raw material mixture in which the magnesium source compound is atomized and uniformly dispersed can be obtained.

方法B: 塗料調整の際、高分散させるためによく用いられるデ
ィスパー分散、ボールミル分散、グレインミル分散等の
方法で、不溶性のマグネシウム源化合物を水に分散さ
せ、得られるマグネシウム源化合物の高分散スラリー液
中にホウ素源化合物及びフラックスを添加し、混合する
と、マグネシウム源化合物が微粒化、均一分散化された
原料混合物を得ることができる。
Method B: Dispersion, ball mill dispersion, grain mill dispersion, etc., which are often used for high dispersion during paint preparation, are used to disperse an insoluble magnesium source compound in water and obtain a highly dispersed slurry of the magnesium source compound. When the boron source compound and the flux are added to the liquid and mixed, a raw material mixture in which the magnesium source compound is atomized and uniformly dispersed can be obtained.

本発明では、次に上記で得られる原料混合溶液を噴霧
乾燥する。噴霧乾燥手段としては、特に限定がなく、従
来の方法を広く適用できる。
In the present invention, the raw material mixed solution obtained above is then spray-dried. The spray drying means is not particularly limited, and conventional methods can be widely applied.

本発明では、次いで得られる噴霧乾燥物を約10℃/分
以下の速度で850℃前後まで昇温し、この温度で処理す
る。昇温速度が10℃/分より極端に速くなると、マグネ
シウムパイロボレートの生成及び結晶化が急激に進行す
るため、結晶成長が不定方向に起り、長さ、太さの揃っ
た繊維の成長を阻害し、その結果本発明の所期の目的が
達成され得なくなるので、好ましくない(後記比較例2
参照)。また加熱処理の温度は850℃前後であることを
要し、その温度での処理時間は1〜5時間程度が望まし
い。650℃や750℃での加熱処理では、微粒子状ピロホウ
酸マグネシウムが生成するに止まり、本発明の如き長さ
や太さの揃った繊維状ピロホウ酸マグネシウムを得るこ
とは不可能である。
In the present invention, the spray-dried product obtained is then heated to about 850 ° C. at a rate of about 10 ° C./minute or less and treated at this temperature. When the heating rate is much faster than 10 ° C / min, the generation and crystallization of magnesium pyroborate will proceed rapidly, causing the crystal growth to occur in an indefinite direction and hindering the growth of fibers of uniform length and thickness. However, as a result, the intended purpose of the present invention cannot be achieved, which is not preferable (Comparative Example 2 described later).
reference). The temperature of the heat treatment needs to be around 850 ° C., and the treatment time at that temperature is preferably about 1 to 5 hours. By heat treatment at 650 ° C. or 750 ° C., only fine particles of magnesium pyroborate are produced, and it is impossible to obtain fibrous magnesium pyroborate having uniform length and thickness as in the present invention.

発明の効果 本発明の方法によれば、ショットがなく、解繊し易く
且つ長さや太さの揃った品質の良好な繊維状ピロホウ酸
マグネシウムを容易に得ることができる。長さ及び太さ
の揃った繊維は、優れた強化性能を発揮する等の利点を
有し、それ故本発明方法により得られる繊維状ピロホウ
酸マグネシウムは工業的利用価値が大きい。
EFFECTS OF THE INVENTION According to the method of the present invention, fibrous magnesium pyroborate having no shots, easy to be defibrated, and good quality with uniform length and thickness can be easily obtained. Fibers of uniform length and thickness have advantages such as exhibiting excellent reinforcing performance, and therefore the fibrous magnesium pyroborate obtained by the method of the present invention has great industrial utility value.

実施例 以下に実施例及び比較例を掲げて本発明をより一層明
らかにする。
Examples The present invention will be further clarified below with reference to Examples and Comparative Examples.

実施例1 酸化マグネシウム8.06gに4M−塩酸水溶液0.1を添加
して溶解した後、溶液を攪拌しながら2M−水酸化カリウ
ム水溶液0.2lを徐々に添加して中和し、コロイド状の水
酸化マグネシウムを生成させる。次いでこれにオルトホ
ウ酸18.55g及び塩化カリウム22.37gを添加し、攪拌して
溶解させる。この混合溶液を、ヤマト科学ミニスプレー
DL−21により噴霧乾燥して、Mg、B及びKClの原料混合
物を製造した。この原料混合物は、電子顕微鏡による観
察の結果、直径3〜10μm程度の微粒子で、その中にMg
はほぼ均一に分布していた。また、X線回折の結果、Mg
及びBについては無定形であった。
Example 1 4M-hydrochloric acid aqueous solution 0.1 was added to 8.06 g of magnesium oxide and dissolved, and then 2M-potassium hydroxide aqueous solution 0.2l was gradually added to the solution while stirring to neutralize the solution to obtain colloidal magnesium hydroxide. Is generated. Next, 18.55 g of orthoboric acid and 22.37 g of potassium chloride are added thereto, and they are dissolved by stirring. This mixed solution is Yamato Scientific Mini Spray
A raw material mixture of Mg, B and KCl was prepared by spray drying with DL-21. As a result of observation with an electron microscope, this raw material mixture is fine particles with a diameter of about 3 to 10 μm, in which Mg
Were distributed almost uniformly. In addition, as a result of X-ray diffraction, Mg
A and B were amorphous.

上記原料混合物の50gをアルミナるつぼに充填し、850
℃まで昇温し(650〜850℃の温度領域での昇温速度10℃
/分)、850℃に3時間保ち、加熱処理した。焼成物
は、熱水中で煮沸してKClを溶解除去した後、水洗、乾
燥した。その結果直径が0.3μm前後、平均繊維長15μ
mのショットを含まない所望の繊維状ピロホウ酸マグネ
シウム8.7gが得られた。この繊維状ピロホウ酸マグネシ
ウムの電子顕微鏡写真を第1図に示す。尚、該繊維の平
均繊維長は、ルーゼックスII〔東洋インキ製造社製〕を
用いて測定したものであり、これは以下の実施例におい
ても同じである。
50 g of the above raw material mixture was filled in an alumina crucible, and 850
Temperature rises to ℃ (temperature rise rate of 10 ℃ in the temperature range of 650 to 850 ℃
/ Min), and kept at 850 ° C. for 3 hours for heat treatment. The baked product was boiled in hot water to dissolve and remove KCl, washed with water and dried. As a result, the diameter is around 0.3 μm and the average fiber length is 15 μm.
8.7 g of the desired fibrous magnesium pyroborate without m shots were obtained. An electron micrograph of this fibrous magnesium pyroborate is shown in FIG. The average fiber length of the fibers was measured using Luzex II (manufactured by Toyo Ink Mfg. Co., Ltd.), and this is the same in the following examples.

実施例2 塩化マグネシウム(MgCl2・6H2O)40.64g及び塩化カ
リウム22.37gの混合水溶液0.1に、ホウ砂(Na2B4O7
10H2O)28.59gの水溶液0.2l、次いで2.5M−水酸化ナト
リウム水溶液0.1を攪拌しながら徐々に添加した後、
上記実施例1と同じ条件で噴霧乾燥、加熱処理を行なっ
た。生成物は、ショットを含まず、直径0.3μm前後、
平均繊維長15μmの所望の繊維状ピロホウ酸マグネシウ
ムであった。
Example 2 In 0.1 of a mixed aqueous solution of 40.64 g of magnesium chloride (MgCl 2 .6H 2 O) and 22.37 g of potassium chloride, borax (Na 2 B 4 O 7
10H 2 O) 0.21 of an aqueous solution of 28.59 g, and then 0.1 parts of 2.5 M sodium hydroxide aqueous solution were gradually added with stirring,
Spray drying and heat treatment were performed under the same conditions as in Example 1 above. The product does not contain shots, has a diameter of around 0.3 μm,
It was the desired fibrous magnesium pyroborate with an average fiber length of 15 μm.

実施例3 酸化マグネシウム16.12gを水0.5l中に分散させ、ボー
ルミルにより高分散させたスラリー液を調製した。調製
されたスラリー液中の酸化マグネシウムの粒子径は3μ
m以下であった。得られたスラリー中にオルトホウ酸3
7.1g及び塩化カリウム44.74gを添加し、攪拌して溶解さ
せた後、650〜850℃の温度領域での昇温速度を5℃/分
とする以外は、上記実施例1と同じ条件で噴霧乾燥、加
熱処理を行なった。生成物は、ショットを含まず、直径
0.3μm前後、平均繊維長12μmの所望の繊維状ピロホ
ウ酸マグネシウムであった。
Example 3 16.12 g of magnesium oxide was dispersed in 0.5 l of water and highly dispersed by a ball mill to prepare a slurry liquid. The particle size of magnesium oxide in the prepared slurry is 3μ
It was m or less. Orthoboric acid 3 in the resulting slurry
7.1 g and 44.74 g of potassium chloride were added, stirred and dissolved, and then sprayed under the same conditions as in Example 1 except that the temperature rising rate in the temperature range of 650 to 850 ° C. was 5 ° C./min. It was dried and heat-treated. Product does not include shot, diameter
It was a desired fibrous magnesium pyroborate having a mean fiber length of about 0.3 μm and 12 μm.

実施例4 実施例1と同様の操作にて得られた原料混合物の50g
をアルミナるつぼに充填し、800℃まで昇温し(650〜80
0℃の温度領域での昇温速度10℃/分)、800℃に4時間
保ち加熱処理した。後処理は実施例1と同様に行ない、
繊維状ピロホウ酸マグネシウム8.7gを得た。得られた繊
維の直径は0.2μm前後で、平均繊維長は10μmであ
り、ショットを含まない所望の繊維状ピロホウ酸マグネ
シウムであった。
Example 4 50 g of the raw material mixture obtained by the same operation as in Example 1
In an alumina crucible and heated to 800 ° C (650-80 ° C).
The temperature was raised in the temperature range of 0 ° C. at a rate of 10 ° C./min) and the temperature was kept at 800 ° C. for 4 hours for heat treatment. The post-treatment is performed in the same manner as in Example 1,
8.7 g of fibrous magnesium pyroborate was obtained. The diameter of the obtained fiber was around 0.2 μm, the average fiber length was 10 μm, and it was a desired fibrous magnesium pyroborate containing no shot.

実施例5 実施例1と同様の操作にて得られた原料混合物の50g
をアルミナるつぼに充填し、900℃まで昇温し(650〜90
0℃の温度領域での昇温速度10℃/分)、900℃に2時間
保ち加熱処理した。後処理は実施例1と同様に行ない、
繊維状ピロホウ酸マグネシウム8.7gを得た。得られた繊
維の直径は0.6μm前後で、平均繊維長は25μmであ
り、ショットを含まない所望の繊維状ピロホウ酸マグネ
シウムであった。
Example 5 50 g of the raw material mixture obtained by the same operation as in Example 1
In an alumina crucible and heated to 900 ° C (650-90
The temperature was raised in the temperature range of 0 ° C. at a rate of 10 ° C./min) and kept at 900 ° C. for 2 hours for heat treatment. The post-treatment is performed in the same manner as in Example 1,
8.7 g of fibrous magnesium pyroborate was obtained. The diameter of the obtained fiber was about 0.6 μm, the average fiber length was 25 μm, and it was a desired fibrous magnesium pyroborate containing no shot.

比較例1 上記実施例1の原料混合比において、酸化マグネシウ
ム8.06gを可溶化することなく、そのままの形でオルト
ホウ酸18.55g及び塩化カリウム52.19gを乳鉢にて十分混
合した。この原料混合物50gを実施例1と同じ条件で処
理した結果、生成物9.3gを得た。この生成物は、直径0.
3μm前後の繊維状ピロホウ酸マグネシウムの他に、直
径10〜30μm程度のショットをかなりの比率で含んでい
た。この生成物の電子顕微鏡写真を第2図に示す。
Comparative Example 1 In the raw material mixing ratio of Example 1 above, 18.55 g of orthoboric acid and 52.19 g of potassium chloride were sufficiently mixed in a mortar without solubilizing 8.06 g of magnesium oxide. As a result of treating 50 g of this raw material mixture under the same conditions as in Example 1, 9.3 g of a product was obtained. This product has a diameter of 0.
In addition to fibrous magnesium pyroborate having a diameter of about 3 μm, a considerable proportion of shots having a diameter of about 10 to 30 μm were included. An electron micrograph of this product is shown in FIG.

比較例2 上記実施例1と全く同じ条件で調製した原料混合物約
50gを充填したアルミナるつぼを、予め850℃に保った電
気炉内へ挿入して急激に加熱した後、850℃で3時間反
応させた。焼成物を実施例1と同じ条件で処理した結
果、8.1gの生成物を得た。該生成物には、ショットは含
まれなかったが、幅10μm以上の柱状乃至板状晶であっ
た。この生成物の電子顕微鏡写真を第3図に示す。
Comparative Example 2 About the raw material mixture prepared under exactly the same conditions as in Example 1 above
An alumina crucible filled with 50 g was inserted into an electric furnace previously kept at 850 ° C., heated rapidly, and then reacted at 850 ° C. for 3 hours. The calcined product was treated under the same conditions as in Example 1, resulting in 8.1 g of product. The product contained no shots, but had columnar or plate-like crystals with a width of 10 μm or more. An electron micrograph of this product is shown in FIG.

【図面の簡単な説明】[Brief description of drawings]

第1図は、実施例1で得られた繊維状ピロホウ酸マグネ
シウムの繊維の形状を示す電子顕微鏡写真である。第2
図は、比較例1で得られたショットを含む繊維状ピロホ
ウ酸マグネシウムの繊維の形状を示す電子顕微鏡写真で
ある。第3図は、比較例2で得られた繊維状ピロホウ酸
マグネシウムの繊維の形状を示す電子顕微鏡写真であ
る。
FIG. 1 is an electron micrograph showing the shape of the fibers of the fibrous magnesium pyroborate obtained in Example 1. Second
The figure is an electron micrograph showing the shape of the fibers of the fibrous magnesium pyroborate containing the shot obtained in Comparative Example 1. FIG. 3 is an electron micrograph showing the fiber shape of the fibrous magnesium pyroborate obtained in Comparative Example 2.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 小川 淳 徳島県徳島市川内町加賀須野463番地 大塚化学株式会社徳島工場内 審査官 雨宮 弘治 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Jun Ogawa 463 Kagasuno, Kawauchi Town, Tokushima City, Tokushima Prefecture Otsuka Chemical Co., Ltd. Tokushima Factory Examiner Koji Amemiya

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】繊維状ピロホウ酸マグネシウムを製造する
に当り、マグネシウム源化合物、ホウ素源化合物及びフ
ラックスを含有し且つマグネシウム源化合物を微粒化し
て原料混合物中に均一に分散させた原料混合溶液を噴霧
乾燥し、次いで得られる噴霧乾燥物を約10℃/分以下の
速度で850℃前後まで昇温し、この温度で処理すること
を特徴とする繊維状ピロホウ酸マグネシウムの製造方
法。
1. A raw material mixed solution containing a magnesium source compound, a boron source compound and a flux, which is atomized and uniformly dispersed in a raw material mixture, in producing fibrous magnesium pyroborate. A method for producing fibrous magnesium pyroborate, which comprises drying, then heating the resulting spray-dried product to a temperature of about 850 ° C. at a rate of about 10 ° C./minute or less, and treating at this temperature.
JP63041726A 1988-02-23 1988-02-23 Method for producing fibrous magnesium pyroborate Expired - Lifetime JP2522981B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63041726A JP2522981B2 (en) 1988-02-23 1988-02-23 Method for producing fibrous magnesium pyroborate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63041726A JP2522981B2 (en) 1988-02-23 1988-02-23 Method for producing fibrous magnesium pyroborate

Publications (2)

Publication Number Publication Date
JPH01215709A JPH01215709A (en) 1989-08-29
JP2522981B2 true JP2522981B2 (en) 1996-08-07

Family

ID=12616427

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Country Status (1)

Country Link
JP (1) JP2522981B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03203961A (en) * 1989-12-29 1991-09-05 Agency Of Ind Science & Technol Thermoplastic resin composition

Also Published As

Publication number Publication date
JPH01215709A (en) 1989-08-29

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