JP2000246127A - Method for grinding metallic hydroxide and production of metallic hydroxide for resin filler by using the method - Google Patents
Method for grinding metallic hydroxide and production of metallic hydroxide for resin filler by using the methodInfo
- Publication number
- JP2000246127A JP2000246127A JP5698199A JP5698199A JP2000246127A JP 2000246127 A JP2000246127 A JP 2000246127A JP 5698199 A JP5698199 A JP 5698199A JP 5698199 A JP5698199 A JP 5698199A JP 2000246127 A JP2000246127 A JP 2000246127A
- Authority
- JP
- Japan
- Prior art keywords
- hydroxide
- metal hydroxide
- air
- metallic hydroxide
- ball mill
- 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
Landscapes
- Crushing And Grinding (AREA)
- Disintegrating Or Milling (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は金属水酸化物の粉砕
方法およびその方法を用いる樹脂充填用金属水酸化物の
製造方法に関する。詳細には、乾式ボールミルを用いて
粗粒の少ない金属水酸化物を得る為の金属水酸化物の粉
砕方法およびその方法を用いる人工大理石等の樹脂充填
用金属水酸化物の製造方法に関する。The present invention relates to a method for pulverizing a metal hydroxide and a method for producing a metal hydroxide for filling a resin using the method. More specifically, the present invention relates to a method of pulverizing a metal hydroxide for obtaining a metal hydroxide with less coarse particles using a dry ball mill and a method of producing a metal hydroxide for filling a resin such as artificial marble using the method.
【0002】[0002]
【従来の技術】水酸化アルミニウム、水酸化マグネシウ
ム等の金属水酸化物は、樹脂、ゴムの充填剤として広く
使用されている。これら金属水酸化物に対する平均粒子
径等の要求物性は、壁紙、カーペット、塗料、電線樹
脂、発泡樹脂、人工大理石、ゴム等用途によって異な
る。所望の要求物性を有する金属水酸化物を得る方法と
して粉砕法がある。2. Description of the Related Art Metal hydroxides such as aluminum hydroxide and magnesium hydroxide are widely used as fillers for resins and rubbers. The required physical properties such as the average particle size of these metal hydroxides vary depending on applications such as wallpaper, carpet, paint, electric wire resin, foamed resin, artificial marble, and rubber. There is a pulverization method as a method for obtaining a metal hydroxide having desired required physical properties.
【0003】金属水酸化物粉砕の為の各種粉砕機が開発
され市販されている。中でも乾式ボールミルは広範囲に
使用されている。Various pulverizers for pulverizing metal hydroxide have been developed and are commercially available. Above all, dry ball mills are widely used.
【0004】しかし、従来、乾式ボールミルを用いる粉
砕方法で金属水酸化物を粉砕する場合には再凝集等が発
生し、得られる金属水酸化物へ粗大粒子が混入する問題
があった。However, conventionally, when a metal hydroxide is pulverized by a pulverization method using a dry ball mill, reaggregation or the like occurs, and there is a problem that coarse particles are mixed into the obtained metal hydroxide.
【0005】[0005]
【発明が解決しようとする課題】かかる事情下に鑑み、
本発明者等は製品への粗大粒子の混入を抑制し得るボー
ルミルを用いる粉砕方法及び樹脂充填用金属水酸化物の
製造方法について鋭意検討を重ねた結果、ボールミルへ
特定量の空気を導入することにより、かかる課題を全て
解決し得ることを見い出し本発明を完成するに至った。In view of such circumstances,
The present inventors have conducted intensive studies on a pulverizing method using a ball mill and a method for producing a metal hydroxide for resin filling that can suppress the incorporation of coarse particles into the product, and as a result, introduce a specific amount of air into the ball mill. As a result, the present inventors have found that all such problems can be solved, and have completed the present invention.
【0006】[0006]
【課題を解決するための手段】即ち、本発明は、金属水
酸化物100容量部と空気100〜3000容量部とを
乾式ボールミル内に連続導入してなる、金属水酸化物の
粉砕方法を提供するにある。That is, the present invention provides a method for pulverizing metal hydroxide by continuously introducing 100 parts by volume of metal hydroxide and 100 to 3000 parts by volume of air into a dry ball mill. To be.
【0007】更に本発明は、金属水酸化物100容量部
と空気100〜3000容量部とを乾式ボールミル内に
連続導入してなる粉砕方法を用いる、樹脂充填用金属水
酸化物の製造方法を提供するにある。Further, the present invention provides a method for producing a metal hydroxide for resin filling using a pulverizing method in which 100 parts by volume of a metal hydroxide and 100 to 3000 parts by volume of air are continuously introduced into a dry ball mill. To be.
【0008】[0008]
【発明の実施の形態】以下、本発明を更に詳細に説明す
る。本発明は、金属水酸化物100容量部と空気100
〜3000容量部とを乾式ボールミル内に連続導入して
なることを特徴とする。空気の量が100容量部より少
ない場合、再凝集等を抑制する効果がなく、得られる製
品に粗大粒子が混入する。空気の量が3000容量部よ
り多い場合、一部金属水酸化物が十分に粉砕されること
なくボールミルから排出されて、製品に粗大粒子が混入
する。また、製品の回収が困難になる場合もある。BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, the present invention will be described in more detail. The invention is based on 100 parts by volume of metal hydroxide and 100 parts by volume of air.
3,000 volume parts is continuously introduced into a dry ball mill. When the amount of air is less than 100 parts by volume, there is no effect of suppressing reagglomeration or the like, and coarse particles are mixed in the obtained product. When the amount of air is more than 3000 parts by volume, some metal hydroxides are discharged from the ball mill without being sufficiently pulverized, and coarse particles are mixed in the product. Also, it may be difficult to collect the product.
【0009】本発明に用いる金属水酸化物は、例えば、
水酸化アルミニウム〔一般式Al2O3・mH2O(式中
m=1〜3)で示される。比重2.42〜3.06〕、
水酸化マグネシウム〔Mg(OH)2、比重2.3
6〕、水酸化カルシウム〔Ca(OH)2、比重2.2
4〕、好ましくはAl2O3・3H2O(比重2.42)
である。また、金属水酸化物は、通常、平均粒子径が約
20μm〜約120μmであり、BET比表面積が1.
5m2/g以下であることが好ましい。The metal hydroxide used in the present invention is, for example,
Aluminum hydroxide [shown by a general formula: Al 2 O 3 · mH 2 O (m = 1 to 3). Specific gravity 2.42 to 3.06],
Magnesium hydroxide [Mg (OH) 2 , specific gravity 2.3
6], calcium hydroxide [Ca (OH) 2 , specific gravity 2.2
4], preferably Al 2 O 3 .3H 2 O (specific gravity 2.42)
It is. The metal hydroxide usually has an average particle size of about 20 μm to about 120 μm and a BET specific surface area of 1.
It is preferably at most 5 m 2 / g.
【0010】本発明に用いる乾式ボールミルは、化学工
学便覧 改訂五版 第829頁〜第834頁(丸善株式
会社、昭和63年3月18日発行)の分類に従えば、連
続式ボールミルであればよく、例えば転動ボールミル、
振動ボールミル、遊星ボールミル等、好ましくは振動ボ
ールミルが挙げられる。また、乾式ボールミルには金属
水酸化物をミル内へ導入する粉体供給装置等に加えて、
空気をミル内へ導入するために、空気圧縮機又は空気ボ
ンベ等空気供給装置が配管を介して連接されている。ミ
ル内への空気の導入方法は、例えば、金属水酸化物と並
流方向又は向流方向、好ましくは並流方向になるように
空気供給装置から配管を介してミル内へ空気を導入すれ
ばよい。According to the classification in the Chemical Engineering Handbook, Revised 5th Edition, pages 829 to 834 (Maruzen Co., Ltd., issued March 18, 1988), a dry ball mill used in the present invention is a continuous ball mill. Well, for example rolling ball mill,
Vibration ball mills, planetary ball mills and the like, preferably vibration ball mills are exemplified. In addition, in addition to the powder supply device that introduces metal hydroxide into the mill,
In order to introduce air into the mill, an air supply device such as an air compressor or an air cylinder is connected via piping. The method of introducing air into the mill is, for example, by introducing air into the mill through a pipe from an air supply device so as to be in a cocurrent or countercurrent direction with the metal hydroxide, preferably in a cocurrent direction. Good.
【0011】粉砕条件は、金属水酸化物の種類、所望と
する平均粒子径、ボールミルの種類等により異なり一義
的ではないが、通常、粉砕温度が約40℃〜約120
℃、好ましくは約60℃〜100℃であり、粉砕時間
(=ボールミル内の金属水酸化物の平均滞留時間)が約
5分〜200分であり、粉砕媒体は直径約1mm〜80
mmのボール、好ましくは5mm〜30mmのボールで
あり、粉砕媒体の見掛充填量はボールミル容積に対して
約30%〜約95%、好ましくは約50%〜90%であ
る。尚、粉砕時間等は所望とする金属水酸化物の平均粒
子径等に応じて予備粉砕実験を行うことにより容易に求
めることが可能である。The pulverization conditions are different depending on the kind of the metal hydroxide, the desired average particle diameter, the kind of the ball mill and the like, and are not unique, but usually, the pulverization temperature is about 40 ° C. to about 120 ° C.
C., preferably about 60 ° C. to 100 ° C., the grinding time (= average residence time of the metal hydroxide in the ball mill) is about 5 minutes to 200 minutes, and the grinding medium has a diameter of about 1 mm to 80 minutes.
mm ball, preferably 5 mm to 30 mm ball, wherein the apparent loading of the grinding media is about 30% to about 95%, preferably about 50% to 90%, based on the ball mill volume. The pulverization time and the like can be easily determined by conducting a preliminary pulverization experiment according to the desired average particle size of the metal hydroxide and the like.
【0012】本発明の金属水酸化物の粉砕方法を行うに
際しては、例えば、水酸化アルミニウム等金属水酸化物
と空気供給装置による空気とを連続式振動ボールミル内
に連続導入し、金属水酸化物を前記ボールミル内に滞留
させて粉砕した後、粉砕された金属水酸化物を回収すれ
ばよく、本発明の樹脂充填用金属水酸化物の製造方法を
行うに際しては、例えば、水酸化アルミニウム等金属水
酸化物と空気供給装置の空気とを連続式振動ボールミル
内に連続導入し、得られる樹脂充填用金属水酸化物の平
均粒子径が所望の値となるように、金属水酸化物を所定
時間前記ボールミル内に滞留させて粉砕した後、粉砕さ
れた金属水酸化物を回収すればよい。In carrying out the metal hydroxide pulverizing method of the present invention, for example, a metal hydroxide such as aluminum hydroxide and air from an air supply device are continuously introduced into a continuous vibration ball mill, and the metal hydroxide is pulverized. Is retained in the ball mill and pulverized, and then the pulverized metal hydroxide may be recovered.When the method for producing a metal hydroxide for resin filling of the present invention is performed, for example, a metal such as aluminum hydroxide may be used. The hydroxide and the air from the air supply device are continuously introduced into the continuous vibration ball mill, and the metal hydroxide is allowed to flow for a predetermined time so that the average particle diameter of the obtained metal hydroxide for resin filling has a desired value. After being retained in the ball mill and pulverized, the pulverized metal hydroxide may be recovered.
【0013】また、本発明の効果を失わない範囲におい
て、同時に前記ボールミル内へ表面処理剤を導入して、
金属水酸化物を表面処理することも可能である。前記表
面処理剤としては、例えば、メタクリル系、アクリル
系、ビニル系、エポキシ系、シラン又はアミノ系シラン
カップリング剤等が挙げられる。表面処理剤の添加量
は、通常、金属水酸化物100重量部に対し約0.1重
量部〜約3重量部である。[0013] In addition, as long as the effects of the present invention are not lost, a surface treating agent is simultaneously introduced into the ball mill,
It is also possible to surface-treat the metal hydroxide. Examples of the surface treatment agent include methacrylic, acrylic, vinyl, epoxy, silane and amino silane coupling agents. The amount of the surface treatment agent is usually about 0.1 part by weight to about 3 parts by weight based on 100 parts by weight of the metal hydroxide.
【0014】本発明の樹脂充填用金属水酸化物の製造方
法において得られる樹脂充填用金属水酸化物は、通常、
平均粒子径が約1μm〜約40μm、好ましくは約5μ
m〜30μmである。平均粒子径が上記範囲を外れる場
合には、前記樹脂充填用金属水酸化物の樹脂への充填性
が低下する傾向にある。また、本発明で得られる樹脂充
填用金属水酸化物は、通常、+45μm量が約5%以下
であり、+106μm量が約0.2重量%以下である。The metal hydroxide for resin filling obtained in the method for producing a metal hydroxide for resin filling of the present invention is usually
Average particle size is about 1 μm to about 40 μm, preferably about 5 μm
m to 30 μm. When the average particle diameter is out of the above range, the filling property of the resin-filling metal hydroxide into the resin tends to decrease. Further, the metal hydroxide for resin filling obtained in the present invention usually has an amount of +45 μm of about 5% or less and an amount of +106 μm of about 0.2% by weight or less.
【0015】前記樹脂充填用金属水酸化物の配合対象と
なる樹脂としては特に制限されないが、水酸化アルミニ
ウムを用いる人工大理石やFRP用途の場合、例えば不
飽和ポリエステル樹脂、ビニルエステル樹脂、メチルメ
タアクリレート樹脂、エポキシ樹脂等が挙げられる。樹
脂中への本発明の水酸化アルミニウムの充填量は、例え
ば樹脂100重量部に対し約50重量部〜約400重量
部、好ましくは約150重量部〜約300重量部の範囲
である。The resin to be compounded with the metal hydroxide for filling the resin is not particularly limited. In the case of artificial marble or FRP using aluminum hydroxide, for example, unsaturated polyester resin, vinyl ester resin, methyl methacrylate Resins, epoxy resins, and the like. The filling amount of the aluminum hydroxide of the present invention in the resin is, for example, about 50 parts by weight to about 400 parts by weight, preferably about 150 parts by weight to about 300 parts by weight, per 100 parts by weight of the resin.
【0016】[0016]
【実施例】以下、本発明を実施例により更に詳細に説明
するが、本発明はかかる実施例により制限を受けるもの
ではない。尚、本実施例に於いて平均粒子径、BET比
表面積は以下の方法により測定した。 平均粒子径(μm) :レーザー散乱式粒度分布計〔リード アンド ノースラップ(LEED&NORTHRUP)社製 マイクロトラックHRA)により測定した。 +45μm量(重量%) :湿式篩別法により測定した。 +106μm量(重量%):湿式篩別法により測定した。 BET比表面積(m2/g):窒素吸着法により測定した。EXAMPLES The present invention will be described in more detail with reference to the following Examples, which should not be construed as limiting the present invention. In this example, the average particle size and the BET specific surface area were measured by the following methods. Average particle diameter (μm): Measured with a laser scattering particle size distribution analyzer (Microtrac HRA manufactured by LEED & NORTHRUUP). +45 μm amount (% by weight): measured by a wet sieving method. +106 μm amount (% by weight): measured by a wet sieving method. BET specific surface area (m 2 / g): measured by a nitrogen adsorption method.
【0017】実施例1 粉体供給装置により平均粒子径が50μmであり、BE
T比表面積が0.2m 2/gであり、比重2.42であ
る水酸化アルミニウム100容量部を、連続式振動ボー
ルミルに配管を介して連接された空気供給装置により空
気530容量部を前記水酸化アルミニウムと並流方向に
なるように連続式振動ボールミル(ボール直径:8m
m、ボール充填率:90%、平均滞留時間:18分)に
連続導入して粉砕し、樹脂充填用水酸化アルミニウムを
得た。得られた樹脂充填用水酸化アルミニウムの物性を
表1に示す。尚、+106μm量は粉砕された金属水酸
化物が再凝集したものであり、+45μm量は金属水酸
化物が十分に粉砕されずにミルから排出されたものであ
る。Example 1 BE powder having an average particle diameter of 50 μm was measured using a powder feeder.
T specific surface area is 0.2m Two/ G and specific gravity of 2.42
100 parts by volume of aluminum hydroxide
Air is connected to the air mill via piping.
530 parts by volume in the direction of cocurrent with the aluminum hydroxide
A continuous vibration ball mill (ball diameter: 8m)
m, ball filling rate: 90%, average residence time: 18 minutes)
Continuously introduced and pulverized, aluminum hydroxide for resin filling
Obtained. The physical properties of the obtained aluminum hydroxide for resin filling
It is shown in Table 1. The amount of +106 μm is the amount of ground metal hydroxide.
Are re-aggregated, and the amount of +45 μm
Is discharged from the mill without sufficient grinding.
You.
【0018】実施例2 実施例1において空気の量を530容量部から1230
容量部に変えた以外は実施例1と同様にして行った。得
られた樹脂充填用水酸化アルミニウムの物性を表1に示
す。Example 2 In Example 1, the amount of air was increased from 530 parts by volume to 1230 parts.
The procedure was performed in the same manner as in Example 1 except that the capacitance part was changed. Table 1 shows the physical properties of the obtained aluminum hydroxide for resin filling.
【0019】比較例1 実施例1において空気を導入しなかったことを除けば、
実施例1と同様にして行った。得られた樹脂充填用水酸
化アルミニウムの物性を表1に示す。Comparative Example 1 Except that no air was introduced in Example 1,
Performed in the same manner as in Example 1. Table 1 shows the physical properties of the obtained aluminum hydroxide for resin filling.
【0020】比較例2 実施例1において空気の量を530容量部から3500
容量部に変えた以外は実施例1と同様にして行った。得
られた樹脂充填用水酸化アルミニウムの物性を表1に示
す。Comparative Example 2 In Example 1, the amount of air was increased from 530 parts by volume to 3500 parts.
The procedure was performed in the same manner as in Example 1 except that the capacitance part was changed. Table 1 shows the physical properties of the obtained aluminum hydroxide for resin filling.
【0021】[0021]
【表1】 [Table 1]
【0022】[0022]
【発明の効果】以上、詳述した如く、本発明は、ボール
ミルに空気を導入するといった簡易な方法で、製品への
粗大粒子の混入を抑制し得る金属水酸化物の粉砕方法及
び樹脂充填用金属水酸化物の製造方法を提供するもので
あり、その産業上の利用価値は大である。As described in detail above, the present invention provides a method for pulverizing a metal hydroxide and a resin filling method capable of suppressing the incorporation of coarse particles into a product by a simple method such as introducing air into a ball mill. The present invention provides a method for producing a metal hydroxide, and its industrial utility value is great.
Claims (6)
〜3000容量部とを乾式ボールミル内に連続導入して
なる、金属水酸化物の粉砕方法。1. 100 parts by volume of metal hydroxide and 100 parts of air
A method for pulverizing a metal hydroxide, comprising continuously introducing up to 3000 parts by volume into a dry ball mill.
てミル内へ導入することを特徴とする請求項1記載の金
属水酸化物の粉砕方法。2. The method for crushing metal hydroxide according to claim 1, wherein said air is introduced into the mill from an air supply device via a pipe.
であることを特徴とする請求項1又は2に記載の金属水
酸化物の粉砕方法。3. The method according to claim 1, wherein the metal hydroxide is aluminum hydroxide.
〜3000容量部とを乾式ボールミル内に連続導入して
なる粉砕方法を用いる、樹脂充填用金属水酸化物の製造
方法。4. 100 parts by volume of metal hydroxide and 100 parts of air
A method for producing a metal hydroxide for resin filling, using a pulverization method in which 3,000 volume parts are continuously introduced into a dry ball mill.
てミル内へ導入することを特徴とする請求項4記載の樹
脂充填用金属水酸化物の製造方法。5. The method for producing a metal hydroxide for resin filling according to claim 4, wherein the air is introduced into the mill from an air supply device via a pipe.
であることを特徴とする請求項4又は5に記載の樹脂充
填用金属水酸化物の製造方法。6. The method for producing a metal hydroxide for resin filling according to claim 4, wherein the metal hydroxide is aluminum hydroxide.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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JP5698199A JP2000246127A (en) | 1999-03-04 | 1999-03-04 | Method for grinding metallic hydroxide and production of metallic hydroxide for resin filler by using the method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5698199A JP2000246127A (en) | 1999-03-04 | 1999-03-04 | Method for grinding metallic hydroxide and production of metallic hydroxide for resin filler by using the method |
Publications (1)
Publication Number | Publication Date |
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JP2000246127A true JP2000246127A (en) | 2000-09-12 |
Family
ID=13042693
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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JP5698199A Pending JP2000246127A (en) | 1999-03-04 | 1999-03-04 | Method for grinding metallic hydroxide and production of metallic hydroxide for resin filler by using the method |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6936236B2 (en) | 2000-04-27 | 2005-08-30 | Sumitomo Chemical Company, Limited | Method for producing an inorganic oxide powder |
-
1999
- 1999-03-04 JP JP5698199A patent/JP2000246127A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6936236B2 (en) | 2000-04-27 | 2005-08-30 | Sumitomo Chemical Company, Limited | Method for producing an inorganic oxide powder |
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