JPH01320220A - Magnesium hydroxide and its production - Google Patents
Magnesium hydroxide and its productionInfo
- Publication number
- JPH01320220A JPH01320220A JP15355388A JP15355388A JPH01320220A JP H01320220 A JPH01320220 A JP H01320220A JP 15355388 A JP15355388 A JP 15355388A JP 15355388 A JP15355388 A JP 15355388A JP H01320220 A JPH01320220 A JP H01320220A
- Authority
- JP
- Japan
- Prior art keywords
- magnesium hydroxide
- magnesium
- plane
- soln
- powder
- 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.)
- Pending
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09C—TREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
- C09C1/00—Treatment of specific inorganic materials other than fibrous fillers; Preparation of carbon black
- C09C1/02—Compounds of alkaline earth metals or magnesium
- C09C1/028—Compounds containing only magnesium as metal
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01F—COMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
- C01F5/00—Compounds of magnesium
- C01F5/14—Magnesium hydroxide
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01F—COMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
- C01F5/00—Compounds of magnesium
- C01F5/14—Magnesium hydroxide
- C01F5/22—Magnesium hydroxide from magnesium compounds with alkali hydroxides or alkaline- earth oxides or hydroxides
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Inorganic Chemistry (AREA)
- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野1
本発明は樹脂に配合して樹脂組成物を難燃化するために
用いられる粉末状水酸化マグネシウム及びその製造法に
関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application 1] The present invention relates to powdered magnesium hydroxide that is blended into a resin and used to make the resin composition flame retardant, and a method for producing the same.
[従来の技術1
現在、各種の合成樹脂に対する難燃化の要求は、その各
種の使用分野から強く望まれているが、その中で無害且
つ安価な難燃剤として水酸化マグネシウムや水酸化アル
ミニウムなどの金属水酸化物が用いられている。[Prior art 1] At present, there is a strong demand for flame retardant properties for various synthetic resins due to their various fields of use. Among these, harmless and inexpensive flame retardants such as magnesium hydroxide and aluminum hydroxide are metal hydroxides are used.
しかしながら、−iに水酸化マグネシウムは微細な粒子
が多数アグロメレートシたものであって、これを合成樹
脂に配合しても分散性が著しく悪いので使用できない。However, magnesium hydroxide -i is agglomerated with a large number of fine particles, and even if it is blended into a synthetic resin, the dispersibility is extremely poor, so it cannot be used.
このようなことから、難燃剤としての水酸化マグネシウ
ムは結晶性で且つ粒成長させた六角板状のものが用いら
れる。For this reason, magnesium hydroxide as a flame retardant is used in the form of crystalline, grain-grown hexagonal plates.
難燃剤に用いられる水酸化マグネシウムの製造するには
種々の方法があり、その代表的な方法は水可溶性のマグ
ネシウム塩水溶液にアルカリを加えることからなる。工
業的には、マグネシウム源として海水あるいは苦汁を含
めた塩化マグネシウムが用いられており、また、アルカ
リとして水酸化カルシウム、水酸化ナトリウム等を用い
て中和反応により得られた水酸化マグネシウムを加圧下
で熟成して製品とする。 このようにして得られる水酸
化マグネシウムの製品は粉末X線回折によると[001
1面と[1011面とのピークの強度比[001コ/[
101]は1.6〜8の範囲にあって薄い板状結晶であ
ることが認められている。ところで、樹脂に練り込まれ
た水酸化マグネシウムは空気中の水分及び炭酸ガス等の
作用を受け、塩基性炭酸マグネシウムないし炭酸マグネ
シウムに変化し、難燃剤としての機能が果たせなくなる
ばかりか、電線の表面に白い粉となって吹き出す現象(
チョーキング)が生じて外観を損ねるという固有の欠点
が存在する。There are various methods for producing magnesium hydroxide used as a flame retardant, and a typical method consists of adding an alkali to an aqueous solution of a water-soluble magnesium salt. Industrially, magnesium chloride containing seawater or bittern is used as a magnesium source, and magnesium hydroxide obtained through a neutralization reaction using calcium hydroxide, sodium hydroxide, etc. as an alkali is used under pressure. It is matured and made into a product. According to powder X-ray diffraction, the magnesium hydroxide product thus obtained was [001
Intensity ratio of peaks between plane 1 and plane [1011 [001/[
101] is in the range of 1.6 to 8 and is recognized to be a thin plate-like crystal. By the way, the magnesium hydroxide kneaded into the resin changes to basic magnesium carbonate or magnesium carbonate under the action of moisture in the air and carbon dioxide gas, and not only does it no longer function as a flame retardant, but it also deteriorates on the surface of the wire. Phenomenon where white powder blows out (
There is an inherent drawback that chalking occurs which detracts from the appearance.
[発明が解決しようとする課題]
しかしながら、合成樹脂の添加剤として分散性の良いと
される前記結晶性水酸化マグネシウムであっても、現存
する結晶性水酸化マグネシウムは板状結晶であるため、
分散性が不充分であり、なお改良の余地がある。[Problems to be Solved by the Invention] However, even though the crystalline magnesium hydroxide is said to have good dispersibility as an additive for synthetic resins, the existing crystalline magnesium hydroxide is a plate-like crystal.
The dispersibility is insufficient, and there is still room for improvement.
ところで、樹脂に練り込まれた水酸化マグネシウムは空
気中の水分及び炭酸ガス等の作用を受け、塩基性炭酸マ
グネシウムないし炭酸マグネシウムに変化し、難燃剤と
しての機能が果たせなくなるばかりか、電線の表面に白
い粉となって吹き出す現象(チョーキング)が生じて外
観を損ねるという固有の欠点が存在する。By the way, the magnesium hydroxide kneaded into the resin changes to basic magnesium carbonate or magnesium carbonate under the action of moisture in the air and carbon dioxide gas, and not only does it no longer function as a flame retardant, but it also deteriorates on the surface of the wire. It has the inherent disadvantage that it causes a phenomenon in which white powder blows out (chalking), which impairs the appearance.
固有の欠点である以上、原則的に避けることはできない
が、可及的にこの欠点を小さくすることは可能である。Since it is an inherent drawback, it cannot be avoided in principle, but it is possible to minimize this drawback as much as possible.
即ち、水酸化マグネシウムの単位体積当たりの表面積が
小さければ、外気に晒される比率が小さい、Rtも小さ
いのは球であって、なるべく球に近い水酸化マグネシウ
ムにすれば外界との影響が低減して耐炭酸化性が生じる
と共に分散性も向上することになる。In other words, if the surface area per unit volume of magnesium hydroxide is small, the ratio of exposure to the outside air is small, and the Rt is also small. If magnesium hydroxide is made as close to a sphere as possible, the influence from the outside world will be reduced. This results in improved carbonation resistance and improved dispersibility.
従って、難燃剤としての水酸化マグネシウムにおいて、
安定性及び分散性の改善の要求に伴って可及的に結晶粒
子に厚みのあるものまたは丸味のあるものが要求される
。Therefore, in magnesium hydroxide as a flame retardant,
In line with the demand for improved stability and dispersibility, crystal grains are required to be as thick or round as possible.
[課題を解決するための手段]
本発明者らは叙上の問題点に鑑み鋭意研究の結果、本発
明を完成するに至った。[Means for Solving the Problems] The present inventors have completed the present invention as a result of intensive research in view of the above-mentioned problems.
即ち、本発明は粉末X線回折法における[001]面と
[101]面の回折線の強度比[001]/[1011
が0.7〜1.3の範囲であり且つBET比表面積が1
〜20m’/gであることを特徴とする水酸化マグネシ
ウムに係る。That is, the present invention is based on the intensity ratio [001]/[1011] of the diffraction lines of the [001] plane and the [101] plane in the powder X-ray diffraction method.
is in the range of 0.7 to 1.3 and the BET specific surface area is 1
It relates to magnesium hydroxide characterized in that it is ~20 m'/g.
更に、本発明はアルカリ水溶液中にマグネシウム塩水溶
液を添加して得られる非常に微細な水酸化マグネシウム
をオートクレーブ中で加熱熟成することからなる粉末X
線回折法における[001]面と[1011面の回折線
の強度比[001]/[101,1が0.7〜1.3の
範囲であり且つBET比表面積が1〜20m2/gであ
る水酸゛化マグネシウムの製造法に係る。Furthermore, the present invention provides powder
The intensity ratio [001]/[101,1 of the diffraction lines of the [001] plane and the [1011 plane] in the line diffraction method is in the range of 0.7 to 1.3, and the BET specific surface area is 1 to 20 m / g. Relates to a method for producing magnesium hydroxide.
[作 用]
本発明の水酸化マグネシウムは上述のように扮末法X線
回折法における[0011面と[]、011面の回折線
の強度比[001]/[101]か0.7〜13の範囲
であり且つBET比表面積が1〜20 m2/gである
ことにより特徴付けられる。[Function] As mentioned above, the magnesium hydroxide of the present invention has an intensity ratio of [0011 plane and [] of the diffraction line of the 011 plane, [001]/[101], or 0.7 to 13 in the X-ray diffraction method. and is characterized by a BET specific surface area of 1 to 20 m2/g.
このような特徴を有する水酸化マグネシウムは従来の薄
い六角板状の粒子と異なり、厚みないし丸味のある結晶
性粒子であって、電子項W1鏡観察によっても容易に識
別することができる。Magnesium hydroxide having such characteristics is different from conventional thin hexagonal plate-shaped particles, and is a thick or rounded crystalline particle, which can be easily identified by electron term W1 mirror observation.
従って、従来のものよりも分散性が良好なものとなって
いる。Therefore, the dispersibility is better than the conventional one.
本発明の水酸化マグネシウムの製造法を更に詳述すると
、アルカリ水溶液として水酸化ナトリウム水溶液を使用
し、これに塩化マグネシウム水溶液を添加して得られる
非常に微細な水酸化マグネシウムをオートクレーブ中で
加熱熟成することにより得ることができる。To explain in more detail the method for producing magnesium hydroxide of the present invention, a sodium hydroxide aqueous solution is used as an alkaline aqueous solution, and an extremely fine magnesium hydroxide obtained by adding a magnesium chloride aqueous solution is heated and aged in an autoclave. It can be obtained by
水酸化ナトリウムと塩化マグネシウムの基本反応式は次
の通りである:
2NaOH+MgCb→2NaOH+Mg(○H)2水
酸化ナトリウムは10〜50%濃度の水溶液として用い
ることが好ましい、塩化マグネシウムはMgCl2とし
て8〜35%の水溶液として用いることが好ましい。The basic reaction formula of sodium hydroxide and magnesium chloride is as follows: 2NaOH + MgCb → 2NaOH + Mg (○H) 2 Sodium hydroxide is preferably used as an aqueous solution with a concentration of 10 to 50%, and magnesium chloride has a concentration of 8 to 35% as MgCl2. % aqueous solution.
本発明の水酸化マグネシウムを製造する際には、まず、
アルカリ水溶液例えば水酸化ナトリウムを撹拌装置の付
いた容器に入れ、0〜100℃の温度でマグネシウム塩
水溶液例えば塩化マグネシウムを20分間〜2時間かけ
て添加する0本発明においては、特にマグネシウム塩の
添加量は水酸化ナトリウムに対して2〜10重量%過剰
になる藍とすることが好ましい。When producing the magnesium hydroxide of the present invention, first,
An alkaline aqueous solution, such as sodium hydroxide, is placed in a container equipped with a stirring device, and a magnesium salt aqueous solution, such as magnesium chloride, is added over a period of 20 minutes to 2 hours at a temperature of 0 to 100°C. Preferably, the amount of indigo is in excess of 2 to 10% by weight relative to sodium hydroxide.
以上の反応により得られた微細なゲル状水酸化マグネシ
ウムのスラリーを母液分離することなくオートクレーブ
中で120〜210℃の温度で1〜8時間加熱熟成する
。The fine gel-like magnesium hydroxide slurry obtained by the above reaction is heated and aged in an autoclave at a temperature of 120 to 210° C. for 1 to 8 hours without separating the mother liquor.
このようにオートクレーブ中で処理された水酸化マグネ
シウムの比表面積は熟成温度が高い程小さくなる。時間
の影響は比較的小さいが長時間になるに従って比表面積
が小さくなる傾向にある。The specific surface area of magnesium hydroxide treated in an autoclave decreases as the aging temperature increases. Although the influence of time is relatively small, the specific surface area tends to decrease as the time increases.
また、粉末X41回折法による[001]面と[101
]面のピーク強度比[001]/[101]は1.0±
0.3の範囲にあり、厚みのある結晶粒子となる。In addition, the [001] plane and [101
] The peak intensity ratio [001]/[101] of the plane is 1.0±
It is in the range of 0.3, resulting in thick crystal grains.
熟成後の水酸化マグネシウムは常法に従って母液を分離
、水洗後、必要に応じて表面処理を行ない?過、乾燥、
粉砕して製品とすることができる。After aging, the mother liquor of magnesium hydroxide is separated according to the usual method, washed with water, and then surface treated as necessary. filtration, drying,
It can be crushed into products.
このようにして得られた本発明の水酸化マグネシウムの
結晶粒子を電子顕微鏡で観察すると、従来の結晶性水酸
化マグネシウムが板状結晶であるのに対して本発明の水
酸化マグネシウムは厚みと丸味のある平均粒子径がほぼ
0.1〜2.5μIの範囲にある1次粒子であることが
観察され、樹脂組成物等に対する分散性も良好であり、
樹脂組成物等に配合しても耐チヨーキング性が従来品よ
りも浸れて、好適なものである。When the crystal particles of the magnesium hydroxide of the present invention obtained in this way are observed with an electron microscope, it is found that conventional crystalline magnesium hydroxide has plate-like crystals, whereas the magnesium hydroxide of the present invention has a thick and round shape. It was observed that the primary particles had a certain average particle diameter in the range of approximately 0.1 to 2.5 μI, and the dispersibility in resin compositions etc. was also good.
Even when blended into resin compositions, etc., the yoking resistance is better than that of conventional products, making it suitable.
し実 施 例]
以下に実施例を挙げて本発明の水酸化マグネシウムを更
に説明する。EXAMPLES] The magnesium hydroxide of the present invention will be further explained with reference to Examples below.
火1猶上
撹拌装置の付いた2、5Nの反応容器に50%液体苛性
ソーダ6.08kyを採る。これに水6.08kgを加
えたところ液温が43℃に上昇した6次いで、このアル
カリ液へ純度96%の工業用塩化マグネシウム(M g
C12・6H20)の70%水溶液L2.1.0kg
を約30分間で滴下して微細な水酸化マグネシウムのゲ
ルを調製した。次いで、このスラリーを圧力容器に移し
、170℃に加熱し、8ky/an2の圧力下で6時間
熟成した。冷却し、母液を分離し、P液のClイオン量
がs ppm以下になるまで洗浄した。6.08 ky of 50% liquid caustic soda was placed in a 2.5N reaction vessel equipped with a stirrer. When 6.08 kg of water was added to this, the liquid temperature rose to 43°C. 6 Next, industrial magnesium chloride (Mg
C12・6H20) 70% aqueous solution L2.1.0kg
was added dropwise over about 30 minutes to prepare a fine magnesium hydroxide gel. This slurry was then transferred to a pressure vessel, heated to 170°C, and aged for 6 hours under a pressure of 8ky/an2. After cooling, the mother liquor was separated and washed until the amount of Cl ions in the P solution became less than sp ppm.
一過、洗浄後、120℃で乾燥し、スイングハンマー式
の粉砕機によって粉砕し、水酸化マグネシウムの粉末2
.14kyを得た。この水酸化マグネシウムにつき、B
ET法による比表面積を測定したところ6.1m”/g
であり、粉末X線回折法による測定ではよく発達した結
晶粒子であり、[001,]面によるピークの強度と[
101,]面によるピークの強度との比率[001]/
[101]は1.05であった。After passing through and washing, dry at 120℃ and crush with a swing hammer type crusher to powder magnesium hydroxide.
.. I got 14ky. For this magnesium hydroxide, B
Specific surface area measured by ET method was 6.1 m"/g
As measured by powder X-ray diffraction, it is a well-developed crystal grain, and the intensity of the peak due to the [001,] plane and [
101,] Ratio of the intensity of the peak due to the plane [001]/
[101] was 1.05.
従って、従来の水酸化マグネシウムに比べて結晶粒子と
しての特徴が認められたが、これを電子顕微鏡で観察し
たところ、厚みと丸味のある平均粒子径がほぼ0,5μ
mの範囲にある1次粒子であることが認められた。Therefore, compared to conventional magnesium hydroxide, it was observed that it had characteristics as crystalline particles, but when it was observed with an electron microscope, it was found that the average particle diameter was approximately 0.5 μm with a thickness and roundness.
It was recognized that the particles were primary particles in the range of m.
夫潴−倒」Ll3−
50重量%の液体苛性ソーダ304gを撹拌装置の付い
た2rの容器に仕込み、室温において撹拌しながらMg
Cβ2として11.51重量%の苦汁液1.655gを
45分間かけて添加して微細なゲル状の水酸化マグネシ
ウム分調製した0次いで、このゲル状水酸化マグネシウ
ムを圧力容器に移し、下記の設定圧力に達するまでの昇
温時間を3時間、設定圧力を保持する時間を6時間、そ
の後熱源を切り放冷するプログラムで熟成を行なった0
次いで、常法により冷却後、内容物を取り出し、taを
分離、水洗、−過、乾燥、粉砕した水酸化マグネシウム
を得た。このときの各条件により得られた試料につき熟
成圧力と水酸化マグネシウムの比表面積及び粉末X線回
折による[001]面と[101]面のピークの強度比
の関係を以下の第1表に記載する。Pour 304g of 50% by weight liquid caustic soda into a 2R container equipped with a stirring device, and add Mg while stirring at room temperature.
1.655 g of bittern liquid containing 11.51% by weight as Cβ2 was added over 45 minutes to prepare a fine gel-like magnesium hydroxide.Next, this gel-like magnesium hydroxide was transferred to a pressure vessel, and the following settings were made. Aging was carried out using a program in which the temperature was raised for 3 hours to reach the pressure, the set pressure was maintained for 6 hours, and then the heat source was turned off and the temperature was left to cool.
Next, after cooling in a conventional manner, the contents were taken out, and ta was separated, washed with water, filtered, dried, and ground to obtain magnesium hydroxide. Table 1 below shows the relationship between aging pressure, specific surface area of magnesium hydroxide, and peak intensity ratio of [001] plane and [101] plane by powder X-ray diffraction for samples obtained under each condition. do.
/′
箸−−L−j緊
2 2 106.6 13.2
0.803 4 107.2
10.5 0.824 6
107.6 7.3 0.865
8 1.04.5 6.5
0.966 10 106.9 4
.5 1.017 12 1.0
6.3 3.5 1.068 1
4 106.0 2.9 1.1
4m
撹拌装置の付いた21の反応容器に市販の塩化マグネシ
ウムの70重量%水溶液605.1gを仕込み、室温に
おいて撹拌しながらこの塩化マグネシウム水溶液へ20
重量%の水酸化ナトリウム水溶液760gを定量ポンプ
を使用し、56分間かけて滴下した。得られた水酸化マ
グネシウムの沈澱をオートクレーブに移し、8 、5
kg/ am2の圧力で4時間熟成した。冷却後、オー
トクレーブより内容物を取り出し、母液を分離、水洗、
濾過、乾燥、粉砕して106.5gの水酸化マグネシウ
ム粉末を得た。この得られた粉末につきB E T法に
よる比表面積を測定したところ8.6aa2/gであり
、粉末X線回折法による測定では[001]面と[1,
011面とのピーク強度比[001,]/[101]は
2.37であった。/' Chopsticks--L-j tense 2 2 106.6 13.2
0.803 4 107.2
10.5 0.824 6
107.6 7.3 0.865
8 1.04.5 6.5
0.966 10 106.9 4
.. 5 1.017 12 1.0
6.3 3.5 1.068 1
4 106.0 2.9 1.1
605.1 g of a commercially available 70% by weight aqueous solution of magnesium chloride was placed in a 21 reaction vessel equipped with a 4 m stirrer, and 20 g was added to the magnesium chloride aqueous solution while stirring at room temperature.
Using a metering pump, 760 g of a wt % aqueous sodium hydroxide solution was added dropwise over 56 minutes. The obtained magnesium hydroxide precipitate was transferred to an autoclave, and 8,5
Aged for 4 hours at a pressure of kg/am2. After cooling, remove the contents from the autoclave, separate the mother liquor, wash with water,
Filtration, drying and pulverization yielded 106.5 g of magnesium hydroxide powder. The specific surface area of the obtained powder was measured by the BET method and was found to be 8.6 aa2/g, and the measurement by the powder
The peak intensity ratio [001,]/[101] with respect to the 011 plane was 2.37.
また、このものを電子詔微鏡にて観察したところ厚みの
非常に薄い板状の粒子であることが認められた。When this material was observed using an electronic microscope, it was found that it was a very thin plate-like particle.
比」交−例じし
MgC&、とじて11.51重量%の苦汁1655を撹
拌装置の付いた21の反応容器に仕込み、室温において
撹拌しながらこの苦汁液へ50重量%の液体苛性ソーダ
304gを定量ポンプで41分間かけて滴下した。得ら
れた水酸化マグネシウムの沈澱を母液と共にオー1〜ク
レープに仕込み、1、0 kg/ cm2の圧力で4時
間熟成する。冷却後、内容物を取り出し、母液を分離、
水洗、濾過、乾燥、粉砕して105.3yの水酸化マグ
ネシウム粉末を得た。この粉末のBET法による比表面
積は6.3m2/gであり、また、粉末X線回折法によ
る[001]面と[101]面とのピーク強度比[00
1]/[101]は1.88であった。11.51% by weight of bittern 1655 was charged into a reaction vessel equipped with a stirring device, and 304 g of 50% by weight liquid caustic soda was quantitatively added to this bittern while stirring at room temperature. The mixture was dripped using a pump over a period of 41 minutes. The obtained precipitate of magnesium hydroxide is charged into a crepe together with the mother liquor and aged at a pressure of 1.0 kg/cm2 for 4 hours. After cooling, take out the contents and separate the mother liquor.
Washing with water, filtration, drying and pulverization yielded 105.3y of magnesium hydroxide powder. The specific surface area of this powder by BET method is 6.3 m2/g, and the peak intensity ratio of [001] plane and [101] plane by powder X-ray diffraction method is [00
1]/[101] was 1.88.
[発明の効果]
上述の実施例及び比較例から分かるように塩化マグネシ
ウム水溶液に水酸化ナトリウム水溶液を添加して製造さ
れる従来の水酸化マグネシウムは粉末X線回折法による
測定結果から[001]面が多く配向し、そのピーク強
度が高くなり、水酸化マグネシウム粒子の直径に対する
厚みのないことが観察された。[Effects of the Invention] As can be seen from the above-mentioned Examples and Comparative Examples, conventional magnesium hydroxide produced by adding a sodium hydroxide aqueous solution to a magnesium chloride aqueous solution has a [001] plane as measured by powder X-ray diffraction. It was observed that many of the particles were oriented, the peak intensity was high, and the thickness of the magnesium hydroxide particles was not relative to the diameter.
これに対して本発明ようにアルカリ水溶液にマグネシウ
ム塩水溶液を添加して得られる非常に微細な水酸化マグ
ネシウムを経由した場合には、粉末X線回折法により測
定した[0011面と[101]面とのピーク強度比か
ら分かるように厚みのある発達した結晶粒子が得られる
。On the other hand, in the case of passing through very fine magnesium hydroxide obtained by adding a magnesium salt aqueous solution to an alkaline aqueous solution as in the present invention, the [0011 plane and [101] plane measured by powder X-ray diffraction method. As can be seen from the peak intensity ratio, thick and well-developed crystal grains are obtained.
本発明の水酸化マグネシウムを樹脂組成物等へ配合した
場合に、分散性が良好であり、難燃化剤として好適に作
用し、チョーキング等の問題も解消される。When the magnesium hydroxide of the present invention is blended into a resin composition or the like, it has good dispersibility, acts suitably as a flame retardant, and eliminates problems such as chalking.
特許出願人 日本化学工業株式会社 手続補正害 昭和63年7月25[1Patent applicant Nihon Kagaku Kogyo Co., Ltd. Procedural amendment damage July 25, 1988 [1
Claims (1)
面の回折線の強度比[001]/[101]が0.7〜
1.3の範囲であり且つBET比表面積が1〜20m^
2/gであることを特徴とする水酸化マグネシウム。 2、水酸化マグネシウムが0.1〜2.5μmの電子顕
微鏡観察に基づく1次粒子の平均粒径をもち且つ厚みと
丸味を帯びた粒子である請求項1記載の水酸化マグネシ
ウム。 3、アルカリ水溶液中にマグネシウム塩水溶液を添加し
て得られる非常に微細な水酸化マグネシウムをオートク
レーブ中で加熱熟成することからなる粉末X線回折法に
おける[001]面と[101]面の回折線の強度比[
001]/[101]が0.7〜1.3の範囲であり且
つBET比表面積が1〜20m^2/gである水酸化マ
グネシウムの製造法。4、10〜50重量%水酸化ナト
リウム溶液中へMgCl_2として8〜35重量%の塩
化マグネシウムを、水酸化ナトリウムに対して塩化マグ
ネシウムが2〜10重量%過剰となる量添加して非常に
微細な水酸化マグネシウムスラリーを得、次いで、該ス
ラリーをオートクレーブ中で120〜210℃の温度で
加熱熟成する請求項3記載の水酸化マグネシウムの製造
法。[Claims] 1. [001] plane and [101] in powder X-ray diffraction method
The intensity ratio [001]/[101] of the surface diffraction line is 0.7 to
1.3 and the BET specific surface area is 1 to 20 m^
2/g of magnesium hydroxide. 2. The magnesium hydroxide according to claim 1, wherein the magnesium hydroxide has an average primary particle diameter of 0.1 to 2.5 μm based on electron microscopic observation, and is thick and rounded. 3. Diffraction lines of [001] plane and [101] plane in powder X-ray diffraction method, which involves heating and aging very fine magnesium hydroxide obtained by adding a magnesium salt aqueous solution to an alkaline aqueous solution in an autoclave. The intensity ratio of [
001]/[101] is in the range of 0.7 to 1.3, and the BET specific surface area is in the range of 1 to 20 m^2/g. 4. Add 8-35% by weight of magnesium chloride as MgCl_2 into a 10-50% by weight sodium hydroxide solution in an amount such that magnesium chloride is in excess of 2-10% by weight relative to the sodium hydroxide to form a very fine particle. The method for producing magnesium hydroxide according to claim 3, wherein a magnesium hydroxide slurry is obtained, and then the slurry is heated and aged in an autoclave at a temperature of 120 to 210°C.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15355388A JPH01320220A (en) | 1988-06-23 | 1988-06-23 | Magnesium hydroxide and its production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15355388A JPH01320220A (en) | 1988-06-23 | 1988-06-23 | Magnesium hydroxide and its production |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH01320220A true JPH01320220A (en) | 1989-12-26 |
Family
ID=15565020
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP15355388A Pending JPH01320220A (en) | 1988-06-23 | 1988-06-23 | Magnesium hydroxide and its production |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH01320220A (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0631984A3 (en) * | 1993-05-26 | 1995-04-26 | Duslo Sp | Magnesium hydroxide and process for its preparation. |
| JP2007016153A (en) * | 2005-07-08 | 2007-01-25 | Konoshima Chemical Co Ltd | Magnesium hydroxide flame retardant having high heat resistance, flame retardant resin composition and molded article |
| JP2007016152A (en) * | 2005-07-08 | 2007-01-25 | Konoshima Chemical Co Ltd | Magnesium hydroxide flame retardant having high heat resistance, flame retardant resin composition and molded article |
| JP2007254250A (en) * | 2006-03-27 | 2007-10-04 | Tateho Chem Ind Co Ltd | Highly pure magnesium hydroxide powder and method for producing the same |
| JP2009062214A (en) * | 2007-09-05 | 2009-03-26 | Kanto Denka Kogyo Co Ltd | Magnesium hydroxide fine particles and method for producing the same |
| CN103508474A (en) * | 2012-06-29 | 2014-01-15 | 中国科学院大连化学物理研究所 | Method for preparing magnesium hydroxide flame retardant by microchannel precipitation-hydrothermal process |
| CN104030325A (en) * | 2014-05-15 | 2014-09-10 | 宁波职业技术学院 | Method for preparing magnesium hydroxide by using magnesium chloride hexammoniate |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS52115799A (en) * | 1976-03-25 | 1977-09-28 | Kyowa Kagaku Kougiyou Kk | Magnesiumhydroxide having novel structure intermediate thereof and process for preparing same |
-
1988
- 1988-06-23 JP JP15355388A patent/JPH01320220A/en active Pending
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS52115799A (en) * | 1976-03-25 | 1977-09-28 | Kyowa Kagaku Kougiyou Kk | Magnesiumhydroxide having novel structure intermediate thereof and process for preparing same |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0631984A3 (en) * | 1993-05-26 | 1995-04-26 | Duslo Sp | Magnesium hydroxide and process for its preparation. |
| JP2007016153A (en) * | 2005-07-08 | 2007-01-25 | Konoshima Chemical Co Ltd | Magnesium hydroxide flame retardant having high heat resistance, flame retardant resin composition and molded article |
| JP2007016152A (en) * | 2005-07-08 | 2007-01-25 | Konoshima Chemical Co Ltd | Magnesium hydroxide flame retardant having high heat resistance, flame retardant resin composition and molded article |
| JP2007254250A (en) * | 2006-03-27 | 2007-10-04 | Tateho Chem Ind Co Ltd | Highly pure magnesium hydroxide powder and method for producing the same |
| JP2009062214A (en) * | 2007-09-05 | 2009-03-26 | Kanto Denka Kogyo Co Ltd | Magnesium hydroxide fine particles and method for producing the same |
| CN103508474A (en) * | 2012-06-29 | 2014-01-15 | 中国科学院大连化学物理研究所 | Method for preparing magnesium hydroxide flame retardant by microchannel precipitation-hydrothermal process |
| CN104030325A (en) * | 2014-05-15 | 2014-09-10 | 宁波职业技术学院 | Method for preparing magnesium hydroxide by using magnesium chloride hexammoniate |
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