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JPH0649573B2 - Aluminum hydroxide for artificial marble and manufacturing method thereof - Google Patents
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JPH0649573B2 - Aluminum hydroxide for artificial marble and manufacturing method thereof - Google Patents

Aluminum hydroxide for artificial marble and manufacturing method thereof

Info

Publication number
JPH0649573B2
JPH0649573B2 JP1187080A JP18708089A JPH0649573B2 JP H0649573 B2 JPH0649573 B2 JP H0649573B2 JP 1187080 A JP1187080 A JP 1187080A JP 18708089 A JP18708089 A JP 18708089A JP H0649573 B2 JPH0649573 B2 JP H0649573B2
Authority
JP
Japan
Prior art keywords
aluminum hydroxide
resin
less
measured
viscosity
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
JP1187080A
Other languages
Japanese (ja)
Other versions
JPH0350142A (en
Inventor
幹人 北山
和之 横尾
幸男 小田
康夫 川合
光彦 森平
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.)
Resonac Holdings Corp
Original Assignee
Showa Denko KK
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Showa Denko KK filed Critical Showa Denko KK
Priority to JP1187080A priority Critical patent/JPH0649573B2/en
Priority to KR1019900701210A priority patent/KR0159504B1/en
Priority to EP89911865A priority patent/EP0407595B1/en
Priority to US07/566,474 priority patent/US5130113A/en
Priority to DE68923171T priority patent/DE68923171D1/en
Priority to AU44823/89A priority patent/AU629254B2/en
Priority to PCT/JP1989/001123 priority patent/WO1990008737A1/en
Priority to NZ231482A priority patent/NZ231482A/en
Priority to CA002004673A priority patent/CA2004673C/en
Publication of JPH0350142A publication Critical patent/JPH0350142A/en
Publication of JPH0649573B2 publication Critical patent/JPH0649573B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、水酸化アルミニウムを不飽和ポリエステル樹
脂、アクリル樹脂等に充填して得られるオニックス調、
マーブル調等の人造大理石製造用の水酸化アルミニウム
とその製造方法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial field of application] The present invention provides an onyx tone obtained by filling aluminum hydroxide into an unsaturated polyester resin, an acrylic resin, or the like,
TECHNICAL FIELD The present invention relates to aluminum hydroxide for producing artificial marble such as marble and a method for producing the same.

〔従来の技術〕[Conventional technology]

水酸化アルミニウムを不飽和ポリエステル樹脂やアクリ
ル樹脂に充填し、オニックス調、マーブル調の成形体を
得ることはよく知られている。
It is well known to fill an unsaturated polyester resin or acrylic resin with aluminum hydroxide to obtain an onyx-like or marble-like molding.

最近、成形体の強度、表面平滑性、耐煮沸特性、及びペ
ースト状態におけるフィラーの沈降を改良する目的でフ
ィラーとして粒径の細かい水酸化アルミニウムが使用さ
れるようになってきた。
Recently, aluminum hydroxide having a small particle size has been used as a filler for the purpose of improving the strength, surface smoothness, boiling resistance, and sedimentation of the filler in a paste state of the molded body.

また、BMC(バルクモールディングコンパウンド)及
び、SMC(シートモールディングコンパウンド)のプ
レス成形によって成形体を得るにあたってはプレス時の
樹脂とフィラーの分離を防ぐためにもフィラーとして粒
径の細かい水酸化アルミニウムを用いることが有利であ
る。
In order to obtain a molded product by press molding of BMC (bulk molding compound) and SMC (sheet molding compound), use aluminum hydroxide having a small particle size as a filler to prevent separation of resin and filler at the time of pressing. Is advantageous.

〔発明が解決しようとする課題〕[Problems to be Solved by the Invention]

しかし、粒径の細かい、すなわち、比表面積の大きい水
酸化アルミニウムを樹脂フィラーとして用いた場合、フ
ィラーの樹脂への分散不良や、樹脂充填粘度が高いとい
う問題があり、フィラーの高充填が困難になることは避
けられない。
However, when the particle size is small, that is, when aluminum hydroxide having a large specific surface area is used as the resin filler, there are problems such as poor dispersion of the filler in the resin and high resin filling viscosity, making it difficult to highly fill the filler. It cannot be avoided.

また、比表面積の大きな水酸化アルミニウムをフィラー
とした不飽和ポリエステル樹脂組成物は、水酸化アルミ
ニウムの表面に、硬化促進剤として用いられるナフテン
酸コバルト等の油溶性硬化促進剤がトラップされるので
ゲルタイムが遅延し、生産性が低下し、さらに成形体が
黄色味を帯びるなどの問題がある。
In addition, the unsaturated polyester resin composition having a large specific surface area of aluminum hydroxide as a filler has a gel time because an oil-soluble curing accelerator such as cobalt naphthenate used as a curing accelerator is trapped on the surface of aluminum hydroxide. However, there is a problem in that the productivity is reduced, the molded product becomes yellowish, and the like.

〔課題を解決するための手段〕[Means for Solving the Problems]

発明者は上記の課題を解決すべく鋭意検討を重ねた結
果、粉砕原料である析出水酸化アルミニウムの1次粒子
径が粉砕物の比表面積や樹脂充填粘度に非常に大きな影
響を与えることを見出し、これに基づいて本発明を完成
するに至ったものである。
As a result of intensive studies to solve the above problems, the inventor has found that the primary particle size of precipitated aluminum hydroxide, which is a raw material for pulverization, has a very large effect on the specific surface area and resin filling viscosity of the pulverized material. Based on this, the present invention has been completed.

すなわち、本発明は、比表面積と樹脂充填粘度の低い水
酸化アルミニウム及び目的とする解砕水酸化アルミニウ
ムの平均粒子径にほぼ等しい1次粒子径を持つ2次凝集
した析出水酸化アルミニウムを解砕原料とし、これを解
砕して製造することを特徴とする人造大理石用水酸化ア
ルミニウムの製造法を提供するにある。
That is, the present invention crushes aluminum hydroxide having a low specific surface area and low resin filling viscosity and secondary agglomerated precipitated aluminum hydroxide having a primary particle diameter substantially equal to the average particle diameter of the intended crushed aluminum hydroxide. Another object of the present invention is to provide a method for producing aluminum hydroxide for artificial marble, which is characterized in that the raw material is crushed and produced.

すなわち、本発明の要旨は、沈降法で測定された平均粒
子径が8μmを越え30μm以下、窒素の吸着法で測定さ
れた比表面積が1.5m2/g以下、20℃で10ポイズの粘度
を有する不飽和ポリエステル樹脂 100重量部に水酸化ア
ルミニウム 200重量部を充填した配合物をブルックフィ
ールド型粘度計で35℃にて測定した樹脂充填粘度が1000
ポイズ以下、75μm以上の粒子径をもつ粒子の割合が1
%以下、白色度が95以上であることを特徴とする人造大
理石用水酸化アルミニウム及び加圧解砕法で測定した平
均径が8μmを越え20μm以下の範囲の1次粒子から構
成された平均粒子径が30〜70μmの水酸化アルミニウム
の2次凝集粒を解砕することを特徴とする前記人造大理
石用水酸化アルミニウムの製造方法とを提供することに
ある。
That is, the gist of the present invention is that the average particle size measured by the sedimentation method exceeds 8 μm and 30 μm or less, the specific surface area measured by the nitrogen adsorption method is 1.5 m 2 / g or less, and the viscosity of 10 poise at 20 ° C. 100 parts by weight of unsaturated polyester resin having 200 parts by weight of aluminum hydroxide filled therein was measured with a Brookfield viscometer at 35 ° C. to obtain a resin filling viscosity of 1000.
The ratio of particles having a particle size of less than or equal to 75 μm and less than poise is 1
% Or less, the whiteness is 95 or more, and the average particle diameter composed of primary particles in the range of 20 μm or less and aluminum hydroxide for artificial marble and the average diameter measured by the pressure crushing method. Another object of the present invention is to provide a method for producing aluminum hydroxide for artificial marble, characterized by crushing secondary aggregated particles of aluminum hydroxide having a size of 30 to 70 μm.

ここで、白色度は光電白色度計で測定した値をいう。1
次粒子径の平均形は、0.75t /cm2の圧力で加圧解砕
し、その平均径を空気透過法で測定した値である。
Here, the whiteness means a value measured by a photoelectric whiteness meter. 1
The average form of the secondary particle diameter is a value obtained by crushing under pressure of 0.75 t / cm 2 and measuring the average diameter by the air permeation method.

水酸化アルミニムの2次凝集粒の粉砕方法は、特に限定
しないが、ボールミルなど粉粒体を粉砕する一般的方法
が採用される。
The method for pulverizing the secondary aggregated particles of aluminum hydroxide is not particularly limited, but a general method such as a ball mill for pulverizing powder particles is adopted.

最初に、本発明の水酸化アルミニウムについて数値の限
定理由を説明する。
First, the reasons for limiting the numerical values of the aluminum hydroxide of the present invention will be described.

沈降法で測定した平均粒子径は、8μmを越え30μm以
下の範囲であり、8μm以下では成形体にした時の強
度、表面平滑性などが良好であるが、8μm以下および
30μmを越えると樹脂充填粘度が高くなる。さらに30μ
mを越えると、樹脂ペーストの曳糸性が悪化するため、
注型法により流れ模様人造大理石を製造する際、流れ模
様が途中で切れ易くなる、また、成形体にした時の強
度、表面平滑性が悪化する、加えて、BMC、及び、S
MCのプレス成形時の樹脂とフィラーの分離を防ぐこと
が難かしくなる。
The average particle size measured by the sedimentation method is in the range of more than 8 μm and 30 μm or less. When the average particle size is 8 μm or less, the strength and surface smoothness when formed into a molded article are good, but 8 μm or less and
When it exceeds 30 μm, the resin filling viscosity becomes high. Further 30μ
If m is exceeded, the spinnability of the resin paste will deteriorate, so
When a flow pattern artificial marble is manufactured by the casting method, the flow pattern is easily broken in the middle, and the strength and surface smoothness of the molded product are deteriorated. In addition, BMC and S
It becomes difficult to prevent the separation of the resin and the filler during press molding of the MC.

BET法で測定した比表面積は、 1.5m2/g以下である
ことが必須であり、これを越えると、フィラーの樹脂へ
の分散不良や不飽和ポリエステル樹脂を過酸化物硬化触
媒で硬化させる時のゲルタイムの著しい遅延を招く。樹
脂充填粘度は、1000ポイズ以下であることが必須であ
り、これを越えると、樹脂とフィラーの混練や注型によ
る成形が困難になる、フィラーの充填量を増すことがで
きないため目標とする色感、量感が得られない、また、
BMCなどにおいてはガラス繊維の混入量を増せないた
め、目標とする強度が得られない、フィラーの高充填が
できないためプレス時の流動特性に劣る等の障害が起こ
る。
It is essential that the specific surface area measured by the BET method is 1.5 m 2 / g or less, and if it exceeds this, the dispersion of the filler in the resin or the unsaturated polyester resin when cured with a peroxide curing catalyst Causes a significant delay in gel time. It is essential that the resin filling viscosity is 1000 poise or less, and if it exceeds this, it will be difficult to knead the resin and filler or molding by casting, and the target color cannot be increased because the filling amount of the filler cannot be increased. I don't get a feeling of volume,
In BMC and the like, the amount of glass fiber mixed cannot be increased, so that the target strength cannot be obtained, and high filling of the filler cannot be achieved, resulting in poor flow characteristics during pressing.

75μm以上の粒子径を持つ粒子の割合は1%以下である
ことが必須であり、これを越えると、樹脂ペーストの曳
糸性が悪化するため、注型法により流れ模様人造大理石
を製造する際、流れ模様が途中で切れ易くなる、また、
成形体にした時の表面平滑性が悪化する。
It is essential that the proportion of particles with a particle size of 75 μm or more is 1% or less, and if it exceeds this, the spinnability of the resin paste deteriorates. Therefore, when manufacturing a flow pattern artificial marble by the casting method. , The flow pattern is easy to cut in the middle,
The surface smoothness of the molded product deteriorates.

光電白色度計で測定した白色度は、95以上であることが
必須であり、これ未満では得られる成形体が淡黄色、あ
るいは、薄茶色に着色し、人造大理石に適した良好な色
調のものが得られなくなる。
It is essential that the whiteness measured with a photoelectric whiteness meter is 95 or more, and if the whiteness is less than this, the obtained molded product is colored in a light yellow or light brown color and has a good color tone suitable for artificial marble. Will not be obtained.

次に、本発明の水酸化アルミニウムの製造方法において
被粉砕原料である水酸化アルミニウムの2次凝集粒につ
いて数値の限定理由を説明する。
Next, the reasons for limiting the numerical values of the secondary aggregated particles of aluminum hydroxide, which is the raw material to be crushed in the method for producing aluminum hydroxide of the present invention, will be described.

沈降法で測定した平均粒子径は30〜70μmの範囲内であ
ることが必須であり、30μm未満では粉砕物の粒度分布
が狭くなり過ぎる結果、樹脂充填粘度が上昇し、また、
70μmを越えると、粉砕物の粗粒残分が多くなるため、
表面平滑性に劣り、また、BMC、及び、SMCのプレ
ス成形時の樹脂とフィラーの分離を防ぐことが難かしく
なる。
It is essential that the average particle size measured by the sedimentation method is within the range of 30 to 70 μm, and if it is less than 30 μm, the particle size distribution of the ground product becomes too narrow, resulting in an increase in resin filling viscosity, and
If it exceeds 70 μm, the coarse particle residue of the pulverized product increases,
The surface is inferior in smoothness, and it becomes difficult to prevent the separation of the resin and the filler during press molding of BMC and SMC.

0.75t /cm2の圧力で加圧解砕、その平均径を空気透
過法で測定することで得られた1次粒子平均径は、8μ
mを越え20μm以下であり、この範囲外では、平均径8
μmを越え30μm以下まで粉砕した時の比表面積、及
び、樹脂充填粘度が高くなる。
The average primary particle diameter obtained by crushing under pressure of 0.75 t / cm 2 and measuring the average diameter by the air permeation method is 8 μm.
The average diameter is 8 μm.
The specific surface area when pulverized to more than 30 μm and more than μm, and the resin filling viscosity become high.

水酸化アルミニウムの1次粒子平均径は、詳しくは、次
のような方法で測定する。すなわち、第1図に示すごと
き金型(円筒ルツボ形、直径30mm、深さ50mm)内に、23
℃RH65%の雰囲気下に1時間放置した水酸化アルミニ
ウム15gを装入し、油圧プレスにより0.75t /cm2
圧力で30秒間加圧する。ついで金型内から水酸化アルミ
ニウムを取り出し、樹脂フィルム製の袋に入れ指圧によ
り圧塊をほぐし得られた解砕粉を空気透過法によりその
平均粒子径(ブレーン径)を測定するものである。
Specifically, the average primary particle diameter of aluminum hydroxide is measured by the following method. That is, in a mold (cylindrical crucible type, diameter 30 mm, depth 50 mm) as shown in FIG.
15 g of aluminum hydroxide left for 1 hour in an atmosphere of RH of 65% is charged, and the pressure of 0.75 t / cm 2 is applied for 30 seconds by a hydraulic press. Then, aluminum hydroxide is taken out from the mold, put in a bag made of a resin film to loosen a pressure lump by finger pressure, and the resulting crushed powder is measured for its average particle size (brain size) by an air permeation method.

〔作用〕[Action]

析出水酸化アルミニウムは1次粒子径が、粉砕物の比表
面積や樹脂充填粘度に大きな影響を与える理由は次のよ
うに考えられる 第2図は、平均粒子径70μm、1次粒子平均径25μmの
析出水酸化アルミニウムの、第3図は、これを 5mmφの
アルミナボールを用いた強制攪拌方式のミルで平均粒子
径16μmまで粉砕した水酸化アルミニウムの電子顕微鏡
写真である。第4図は、平均粒子径42μm、1次粒子平
均径15μmの析出水酸化アルミニウムの、第5図は、こ
れを 5mmφのアルミナボールを用いた強制攪拌方式のミ
ルで平均粒子径16μmまで解砕した水酸化アルミニウム
の電子顕微鏡写真である。写真より明らかなように、1
次粒平均径25μmの水酸化アルミニウムを平均粒子径16
μmまで粉砕すると1次粒子の破壊が当然起るため、水
酸化アルミニウムの劈開性により、板状で不定形な粒子
形状となり、その結果、樹脂に高充填した際の粘度が高
くなる。さらに、1次粒子を破壊しなければならないの
で、粉砕時間が長くなり、粒子表面が荒れ、多量のチッ
ピング粒が発生するため、比表面積が大きくなる。これ
に対して、1次粒平均径が15μmの水酸化アルミニウム
を平均粒径16μmまで粉砕することは、いわば、2次凝
集粒の解砕であり、1次粒子の破壊はほとんどなく、解
砕物の粒子形状は、析出水酸化アルミニウムの1次粒子
の丸味を持った粒子形状をよく保っているため、樹脂に
高充填した際の粘度は低い。さらに粉砕時間が短いた
め、比表面積も小さい。
The reason why the primary particle size of the precipitated aluminum hydroxide has a great influence on the specific surface area of the pulverized product and the resin filling viscosity is considered as follows. Fig. 2 shows that the average particle size is 70 μm and the average primary particle size is 25 μm. FIG. 3 of the deposited aluminum hydroxide is an electron micrograph of aluminum hydroxide obtained by pulverizing the aluminum hydroxide to a mean particle size of 16 μm with a forced stirring type mill using alumina balls of 5 mmφ. Fig. 4 shows precipitated aluminum hydroxide having an average particle diameter of 42 µm and primary particle average diameter of 15 µm. It is an electron micrograph of the formed aluminum hydroxide. As is clear from the photograph, 1
The average particle size of aluminum hydroxide with an average particle size of 25 μm is 16
Since crushing of the primary particles naturally occurs when the particles are pulverized to a size of μm, the cleavability of aluminum hydroxide causes a plate-like and irregular particle shape, resulting in an increase in viscosity when highly filled with resin. Further, since the primary particles have to be destroyed, the crushing time becomes long, the particle surface becomes rough, and a large amount of chipping particles are generated, so that the specific surface area becomes large. On the other hand, crushing aluminum hydroxide having an average primary particle diameter of 15 μm to an average particle diameter of 16 μm is, so to speak, crushing of secondary agglomerated particles, and there is almost no destruction of primary particles. As for the particle shape, since the rounded particle shape of the primary particles of the precipitated aluminum hydroxide is well maintained, the viscosity when the resin is highly filled is low. Furthermore, since the crushing time is short, the specific surface area is also small.

〔実施例〕〔Example〕

以下、本発明を第1表に示す実施例、及び第2表に示す
比較例により、具体的に説明するが、表中の樹脂・水酸
化アルミニウム複合組成物の評価は次のように行なっ
た。
Hereinafter, the present invention will be specifically described with reference to Examples shown in Table 1 and Comparative Examples shown in Table 2. Evaluation of the resin / aluminum hydroxide composite composition in the table was performed as follows. .

1.樹脂充填粘度及び 2.分散時間 (配合)不飽和ポリエステル樹脂 1 100部 水酸化アルミニウム 200部 上記配合で攪拌混練を行ない、完全にペースト状になる
までの時間を分散時間とし、その時の粘度(BS型粘度
計使用、35℃)を樹脂充填粘度とする。樹脂充填粘度
は、1000ポイズ以下が好ましく、分散時間は10分以下が
望ましい。
1. Resin filling viscosity and 2. Dispersion time (blending) Unsaturated polyester resin * 1 100 parts Aluminum hydroxide 200 parts Stirring and kneading with the above blending is the time until completely paste-like, and the viscosity at that time (using a BS type viscometer, 35 ° C) is the resin filling viscosity. The resin filling viscosity is preferably 1000 poise or less, and the dispersion time is preferably 10 minutes or less.

*1 昭和高分子社製リゴラック2004WM−2 3.成形体の色調及び 4.ゲルタイム (配合)不飽和ポリエステル樹脂 2 100部 MEKPO(メチル・エチル・ ケトン パーオキサイド商品名 パーメックN日本油脂(株)製) 1部 6%ナフテン酸コバルト 0.2部 水酸化アルミニウム 150部 *2 屈折率1.52、粘度18p(25℃) 上記配合で攪拌混練を行ない、25℃の恒温槽にて、組成
物の粘度を連続して測定し、樹脂の硬化により、粘度が
上昇し始めるまでの時間をゲルタイムとする。
* 1 Showa High Polymer Co., Ltd. Rigolac 2004 WM-2 3. 3. Color tone of molded product and 4. Gel time (blended) unsaturated polyester resin * 2 100 parts MEKPO (Methyl ethyl ketone peroxide trade name Permek N NOF CORPORATION) 1 part 6% cobalt naphthenate 0.2 parts aluminum hydroxide 150 parts * 2 Refractive index 1.52, viscosity 18p (25 ° C) Stir kneading with the above composition, continuously measuring the viscosity of the composition in a constant temperature bath at 25 ° C, the time until the viscosity begins to rise due to resin curing Is the gel time.

ゲルタイムでは、60分以下が好ましい。The gel time is preferably 60 minutes or less.

また、上記配合で脱泡混練を行ない、3mφ×15mm厚の
成形型に注型し、1晩室温(25℃)で硬化後、50℃、3
時間加熱硬化させた硬化物の色調を、スガ試験機(株)製
カラーテスターSM−4−CHで測定し、ハンター色調
座標Labで表わした。これを成形体の色調とする。ハ
ンター色度座標は(L,a,b)で表示され、軸Lは明
度を表わし、a,bは知覚色度指数で側と側があ
り、それぞれ、赤と緑、黄とを表わす。人造大理石とし
ては、黄味を表わすbが重要であり、10以下であること
が好ましい。
Also, defoaming and kneading with the above composition, casting in a 3 mφ × 15 mm thick molding die, and curing at room temperature (25 ° C.) overnight, then at 50 ° C., 3
The color tone of the cured product heat-cured for a period of time was measured with a color tester SM-4-CH manufactured by Suga Test Instruments Co., Ltd. and represented by Hunter color tone coordinates Lab. This is the color tone of the molded body. Hunter chromaticity coordinates are represented by (L, a, b), axis L represents lightness, and a and b are perceptual chromaticity indices having side and side, which represent red, green, and yellow, respectively. As artificial marble, b representing yellow is important, and it is preferably 10 or less.

5.曳糸性 (配合)不飽和ポリエステル樹脂 2 100部 MEKPO(メチル・エチル・ ケトン
パーオキサイド商品名 パーメックN日本油脂
(株)製) 1部 6%ナフテン酸コバルト 0.2部 水酸化アルミニウム粗粒(70μm)70部 水酸化アルミニウム細粒 160部 *2 屈折率1.52、粘度18p(25℃) 上記配合を攪拌混練後、樹脂スラリーをスパチュラです
くい、垂らした時の曳き具合を曳糸性と呼び、次のよう
に判断した。
5. Spinnability (blended) unsaturated polyester resin * 2 100 parts MEKPO (Methyl ethyl ketone peroxide Trade name Permec N Nippon Oil & Fats
1 part 6% Cobalt naphthenate 0.2 part Aluminum hydroxide coarse particles (70 μm) 70 parts Aluminum hydroxide fine particles 160 parts * 2 Refractive index 1.52, viscosity 18p (25 ° C) After stirring and kneading, The resin slurry was scooped with a spatula and the pulling condition when dropped was called the spinnability and judged as follows.

・糸を曳かずに塊状になって垂れる:× ・糸は曳くが途中で切れ易い :△ ・糸を曳き、スムースに垂れる :○ これらの結果より、本発明による細粒水酸化アルミニウ
ムは従来のものに比べ比表面積が小さいので、樹脂への
分散性が良好であり、不飽和ポリエステル樹脂に充填し
た時のゲルタイムの遅延に対する抑制効果があり、成形
体の色調が黄色味を帯びることも少ない、また、樹脂に
充填した際の粘度が低いため高充填が可能である。加え
て粗粒残渣が少ないため曳糸性に優れ、注型法により流
れ模様人造大理石を製造する際、流れ模様が途中で切れ
るということがないことが判る。
・ Drops in a lump without pulling the thread: × ・ Pulls the thread, but it is easy to break in the middle: △ ・ Pulls the thread and drips smoothly: ○ From these results, the fine-grained aluminum hydroxide according to the present invention has a smaller specific surface area as compared with the conventional one, so that the dispersibility in the resin is good, and the suppression effect against the delay of the gel time when the unsaturated polyester resin is filled. Therefore, the color tone of the molded product is less likely to have a yellowish tint, and since the viscosity when filled with the resin is low, high filling is possible. In addition, since there are few coarse-grained residues, the spinnability is excellent, and it is understood that the flow pattern is not cut off in the middle when the flow pattern artificial marble is manufactured by the casting method.

〔発明の効果〕〔The invention's effect〕

かくして得られた水酸化アルミニウムは、特に人造大理
石用フィラーとして、品質設計されたものであり、この
用途に用いられた時にその優れた特性を発揮する。
The aluminum hydroxide thus obtained is quality-designed especially as a filler for artificial marble, and exhibits excellent properties when used in this application.

例えば、不飽和ポリエステル樹脂に充填し、注型法によ
って洗面化粧台やキッチンカウンタートップなどを製造
する際、本発明の水酸化アルミニウムをフィラーとして
用いれば、樹脂への分散性がよいため、攪拌混練が短時
間ですむ。また、コストダウンの目的で樹脂分を減らす
ためにフィラーを高充填しても低粘度であるため、注型
作業が行ない易い。さらに、不飽和ポリエステル樹脂の
硬化時間が従来の細粒水酸化アルミニウムを充填した場
合に比べ、格段に短かいので生産性に優れる。加えて、
硬化物の黄色味が少ないため、顔料を加えない場合に
も、加えた場合にも、美麗な色調の製品が得られる。
For example, when the aluminum hydroxide of the present invention is used as a filler when an unsaturated polyester resin is filled and a vanity or kitchen countertop is manufactured by a casting method, the dispersibility in the resin is good, and thus the mixture is stirred and kneaded. But in a short time. Further, even if the filler is highly filled to reduce the resin content for the purpose of cost reduction, the viscosity is low, and therefore the casting operation is easy to perform. Further, the curing time of the unsaturated polyester resin is remarkably short as compared with the case where conventional fine-grained aluminum hydroxide is filled, so that the productivity is excellent. in addition,
Since the cured product has little yellowness, a product with a beautiful color tone can be obtained with or without the addition of a pigment.

曳糸性に優れるため、美麗な流れ模様人造大理石が得ら
れる。
Due to its excellent spinnability, beautiful flow pattern artificial marble can be obtained.

また、BMCやSMCのプレス成形法によって洗面化粧
台やバスタブなどを製造する際、本発明の水酸化アルミ
ニウムをフィラーと用いれば、高充填が可能であり、プ
レス時の流動特性に優れる。さらに、得られた成形体の
表面平滑性に優れるため、高級感があり、加えて、耐汚
染性にも優れる。
Further, when a vanity, bathtub or the like is manufactured by a BMC or SMC press molding method, if the aluminum hydroxide of the present invention is used as a filler, high filling is possible and the flow characteristics at the time of pressing are excellent. Further, since the obtained molded body has excellent surface smoothness, it has a high-class feeling and, in addition, has excellent stain resistance.

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

第1図は1次粒子平均径測定のための加圧解砕法に使用
する金型の断面図、第2図〜第5図は水酸化アルミニウ
ムの粒子構造を示す電子顕微鏡写真である。
FIG. 1 is a sectional view of a mold used in a pressure crushing method for measuring the average primary particle diameter, and FIGS. 2 to 5 are electron micrographs showing the particle structure of aluminum hydroxide.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 川合 康夫 神奈川県横浜市神奈川区恵比須町8 昭和 電工株式会社横浜工場内 (72)発明者 森平 光彦 神奈川県横浜市神奈川区恵比須町8 昭和 電工株式会社横浜工場内 (56)参考文献 特開 平1−275422(JP,A) ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Yasuo Kawai 8 Ebisu-cho, Kanagawa-ku, Yokohama, Kanagawa Prefecture Showa Denko KK Yokohama factory (72) Inventor Mitsuhiko Morihira 8 Ebisu-cho, Kanagawa-ku, Yokohama, Showa Denko KK Yokohama factory (56) Reference JP-A-1-275422 (JP, A)

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】沈降法で測定された平均粒子径が8μmを
越え30μm以下、窒素の吸着法(BET法)で測定され
た比表面積が 1.5m2/g以下、20℃で10ポイズの粘度を
有する不飽和ポリエステル樹脂 100重量部に水酸化アル
ミニウム 200重量部を充填した配合物をブルックフィー
ルド型粘度計で35℃にて測定した樹脂充填粘度が1000ポ
イズ以下、75μm以上の粒子径をもつ粒子の割合が1%
以下、白色度が95以上であることを特徴とする人造大理
石用水酸化アルミニウム。
1. An average particle diameter of more than 8 μm and less than 30 μm measured by a sedimentation method, a specific surface area of less than 1.5 m 2 / g measured by a nitrogen adsorption method (BET method), and a viscosity of 10 poise at 20 ° C. Particles having a resin filling viscosity of 1000 poise or less and a particle size of 75 μm or more measured by a Brookfield viscometer at 35 ° C. with a mixture of 100 parts by weight of an unsaturated polyester resin containing 200 parts by weight of aluminum hydroxide. Is 1%
Hereinafter, aluminum hydroxide for artificial marble, which has a whiteness of 95 or more.
【請求項2】加圧粉砕法で測定した平均径が8μmを越
え20μm以下の範囲の1次粒子から構成された平均粒子
径が30〜70μmの水酸化アルミニウムの2次凝集粒を解
砕して、請求項1記載の人造大理石用水酸化アルミニウ
ムを製造する方法。
2. A secondary agglomerate of aluminum hydroxide having an average particle diameter of 30 to 70 μm, which is composed of primary particles having an average diameter of more than 8 μm and not more than 20 μm measured by a pressure crushing method, is crushed. A method for producing the aluminum hydroxide for artificial marble according to claim 1.
JP1187080A 1989-01-26 1989-07-19 Aluminum hydroxide for artificial marble and manufacturing method thereof Expired - Lifetime JPH0649573B2 (en)

Priority Applications (9)

Application Number Priority Date Filing Date Title
JP1187080A JPH0649573B2 (en) 1989-07-19 1989-07-19 Aluminum hydroxide for artificial marble and manufacturing method thereof
KR1019900701210A KR0159504B1 (en) 1989-01-26 1989-10-31 Method of manufacturing aluminum hydroxide
EP89911865A EP0407595B1 (en) 1989-01-26 1989-10-31 Aluminum hydroxide, process for its production and composition
US07/566,474 US5130113A (en) 1989-01-26 1989-10-31 Aluminum hydroxide, process for preparation thereof and composition
DE68923171T DE68923171D1 (en) 1989-01-26 1989-10-31 ALUMINUM HYDROXYD, METHOD FOR THE PRODUCTION AND COMPOSITION.
AU44823/89A AU629254B2 (en) 1989-01-26 1989-10-31 Aluminum hydroxide, process for its production and composition
PCT/JP1989/001123 WO1990008737A1 (en) 1989-01-26 1989-10-31 Aluminum hydroxide, process for its production and composition
NZ231482A NZ231482A (en) 1989-01-26 1989-11-22 Aluminium hydroxide and its use in an artificial marble composition
CA002004673A CA2004673C (en) 1989-01-26 1989-12-05 Aluminum hydroxide, process for preparation thereof and composition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1187080A JPH0649573B2 (en) 1989-07-19 1989-07-19 Aluminum hydroxide for artificial marble and manufacturing method thereof

Publications (2)

Publication Number Publication Date
JPH0350142A JPH0350142A (en) 1991-03-04
JPH0649573B2 true JPH0649573B2 (en) 1994-06-29

Family

ID=16199782

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1187080A Expired - Lifetime JPH0649573B2 (en) 1989-01-26 1989-07-19 Aluminum hydroxide for artificial marble and manufacturing method thereof

Country Status (1)

Country Link
JP (1) JPH0649573B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002114867A (en) * 2000-07-17 2002-04-16 Showa Denko Kk Aluminum hydroxide powder for filling resin and resin composition using the same

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP7684118B2 (en) * 2021-07-07 2025-05-27 住友化学株式会社 Aluminum hydroxide powder
CN114436302B (en) * 2022-01-10 2024-08-27 中铝山东新材料有限公司 A kind of microparticle aluminum hydroxide and its preparation method, production system and application

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63291841A (en) * 1987-05-26 1988-11-29 Nippon Shokubai Kagaku Kogyo Co Ltd Artificial marble of good cutting operability
JPH01275422A (en) * 1987-12-21 1989-11-06 Showa Denko Kk Aluminum hydroxide for artificial marble and its production

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002114867A (en) * 2000-07-17 2002-04-16 Showa Denko Kk Aluminum hydroxide powder for filling resin and resin composition using the same

Also Published As

Publication number Publication date
JPH0350142A (en) 1991-03-04

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