JPH07100908A - Production of marblelike molded product - Google Patents

Production of marblelike molded product

Info

Publication number
JPH07100908A
JPH07100908A JP24793093A JP24793093A JPH07100908A JP H07100908 A JPH07100908 A JP H07100908A JP 24793093 A JP24793093 A JP 24793093A JP 24793093 A JP24793093 A JP 24793093A JP H07100908 A JPH07100908 A JP H07100908A
Authority
JP
Japan
Prior art keywords
weight
resin plate
molded product
meth
parts
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
Application number
JP24793093A
Other languages
Japanese (ja)
Inventor
Akihiko Fukada
亮彦 深田
Hiroshi Okamoto
弘 岡本
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.)
Nippon Shokubai Co Ltd
Original Assignee
Nippon Shokubai Co Ltd
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 Nippon Shokubai Co Ltd filed Critical Nippon Shokubai Co Ltd
Priority to JP24793093A priority Critical patent/JPH07100908A/en
Publication of JPH07100908A publication Critical patent/JPH07100908A/en
Pending legal-status Critical Current

Links

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  • Blow-Moulding Or Thermoforming Of Plastics Or The Like (AREA)

Abstract

PURPOSE:To simply and inexpensively produce a deep-draw product having marblelike appearance. CONSTITUTION:20-200 pts.wt. of an inorg. filler and a polymerization initiator are kneaded with 100 pts.wt. of an acrylic resin syrup and the resulting kneaded mixture is polymerized to prepare a thermoplastic resin with a wt. average mol.wt. of 200000-1500000. This resin is molded into a thermoplastic resin plate with a thickness of 1-15mm and this plate is subjected to vacuum and/or pressure forming to produce a molded product having marblelike appearance.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は大理石調の外観を持つ成
形品を真空および/または圧空成形により作成する製造
方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a molded article having a marble-like appearance by vacuum and / or pressure forming.

【0002】[0002]

【従来の技術】従来、多量の無機質充填剤を配合したア
クリル樹脂成形品の製造は主に注型により行われてお
り、大理石調の外観を持つキッチンカウンタートップ、
洗面ボール、机上パネル等に使用されている。例えば特
開平4−345812号にはアクリルシロップと無機質
充填剤の配合物の注型による異形成形品の製造方法が開
示されている。しかし、これらの用途に応じた成形品形
状に注型成形する方法では生産性が低く、また、注型成
形時にクラックが発生しやすく歩溜まりが悪い等、コス
ト面での問題が大きい。
2. Description of the Related Art Conventionally, acrylic resin moldings containing a large amount of inorganic filler have been mainly produced by casting, and kitchen countertops with a marble-like appearance,
It is used for wash-basins and desk panels. For example, Japanese Patent Application Laid-Open No. 4-345812 discloses a method for producing a shaped article by casting a mixture of an acrylic syrup and an inorganic filler. However, the method of cast molding into the shape of a molded product according to these uses has low productivity, and cracks are likely to occur during cast molding, resulting in poor yield.

【0003】[0003]

【発明が解決しようとする課題】無機質充填剤を配合し
たアクリル樹脂板を真空および/または圧空成形によっ
て平板以外の成形品を作成しようとすると無機質充填剤
の量や大きさ、アクリル樹脂の分子量、板厚などに制約
がある。例えば、多量の無機質充填剤を配合した場合樹
脂板の剛性が増大し、マトリックス樹脂の軟化点以上に
加熱しても充分な伸張性を示さず真空および/または圧
空成形することは困難となる。逆に、無機質充填剤が少
なすぎると重合中に充填剤の沈降の問題や、また樹脂板
の大理石調の外観が損なわれるといった問題が生じる。
また、高充填にしても樹脂板の剛性が増大し過ぎないよ
うにするためポリマーの分子量を低減する事が考えられ
るが、低分子量ポリマーをマトリックスとした高充填樹
脂板を真空および/または圧空成形すると成形品の肉厚
分布が大きくなったり伸張性が少ないという問題が生じ
る。逆に、重量平均分子量が150万を超える高分子量
ポリマーをマトリックストした高充填樹脂板は先にも述
べた通り剛性が高く軟化点も上昇して予熱中にポリマー
の解重合を引き起こす。更に、板厚が大きくなるほど加
熱時の伸張に大きな力が必要となり真空および/または
圧空成形しにくくなる。
When an acrylic resin plate mixed with an inorganic filler is subjected to vacuum and / or pressure forming to make a molded product other than a flat plate, the amount and size of the inorganic filler, the molecular weight of the acrylic resin, There are restrictions on plate thickness. For example, when a large amount of an inorganic filler is added, the rigidity of the resin plate increases, and even if the resin plate is heated above the softening point of the matrix resin, sufficient extensibility is not exhibited, and vacuum and / or pressure forming becomes difficult. On the other hand, when the amount of the inorganic filler is too small, there arises a problem that the filler is settled during the polymerization and a problem that the marble-like appearance of the resin plate is impaired.
Also, it is possible to reduce the molecular weight of the polymer so that the rigidity of the resin plate does not increase too much even if it is highly filled, but vacuum and / or air pressure molding of a highly filled resin plate using a low molecular weight polymer as a matrix Then, there arises a problem that the thickness distribution of the molded product becomes large and the extensibility is small. On the contrary, the highly filled resin plate in which a high molecular weight polymer having a weight average molecular weight of more than 1,500,000 is matrixed has high rigidity and a high softening point as described above, and causes depolymerization of the polymer during preheating. Furthermore, as the plate thickness increases, a larger force is required for stretching during heating, which makes vacuum and / or pressure air molding difficult.

【0004】本発明はかかる現状の問題の改良を目的と
するものであって、大理石調の外観を持った深絞り成形
品の製造方法を提供するものである。
[0004] The present invention is intended to improve the present problems, and provides a method for producing a deep-drawn molded product having a marble-like appearance.

【0005】本発明者らが種々検討した結果、無機質充
填剤を特定量配合し、マトリックス樹脂の分子量を特定
範囲内になるように制御して重合せしめた特定の板厚を
もつ注型板を用いることによって大理石調の外観を有
し、且つ熱成形による深絞り成形品の製造が可能となる
ことを見いだして本発明を完成させたものである。
As a result of various studies by the present inventors, a casting plate having a specific plate thickness prepared by compounding a specific amount of an inorganic filler and controlling the molecular weight of the matrix resin to fall within a specific range and polymerizing the mixture. The present invention has been completed by finding that by using it, it is possible to produce a deep-drawing molded product by thermoforming and having a marble-like appearance.

【0006】[0006]

【課題を解決するための手段】本発明は(メタ)アクリ
ル系ポリマーと(メタ)アクリル系モノマーから成るア
クリルシロップ100重量部に対し、無機質充填剤20
〜200重量部および硬化剤を混合して成る配合物を重
合して重量平均分子量が20万〜150万で、厚みが1
〜15mmの平板状熱可塑性樹脂板を成形し、得られた
樹脂板を軟化点以上に加熱した状態で真空および/また
は圧空成形し、大理石調外観を持つ成形品を製造する方
法に関するものである。
According to the present invention, an inorganic filler 20 is added to 100 parts by weight of an acrylic syrup consisting of a (meth) acrylic polymer and a (meth) acrylic monomer.
~ 200 parts by weight and a curing agent are mixed to polymerize a mixture to give a weight average molecular weight of 200,000 to 1,500,000 and a thickness of 1
TECHNICAL FIELD The present invention relates to a method for producing a molded product having a marble-like appearance by forming a flat thermoplastic resin plate having a thickness of up to 15 mm, and vacuum and / or pressure forming the obtained resin plate in a state of being heated to a softening point or higher. .

【0007】該成形品は無機質充填剤が沈降することな
く大理石調外観を保持し、また真空および/または圧空
成形後も肉厚分布が比較的小さい。また、機械的強度や
表面の耐汚染性にも優れている。
The molded product retains a marble-like appearance without sedimentation of the inorganic filler, and has a relatively small wall thickness distribution after vacuum and / or pressure molding. It also has excellent mechanical strength and resistance to surface contamination.

【0008】本発明に使用されるアクリルシロップとは
例えば、メチル(メタ)アクリレート、エチル(メタ)
アクリレート、ブチル(メタ)アクリレート、プロピル
(メタ)アクリレート、オクチル(メタ)アクリレー
ト、2−エチルヘキシル(メタ)アクリレート、ラウリ
ル(メタ)アクリレート、ステアリル(メタ)アクリレ
ート等のアルキル(メタ)アクリレートモノマーのうち
1種または2種以上と、上記モノマーのうち1種または
2種以上を原料としたポリアルキル(メタ)アクリレー
トとの混合物から成る。また、モノマーの一部をエチレ
ングリコールジ(メタ)アクリレート、ポリエチレング
リコールジ(メタ)アクリレート、プロピレングリコー
ルジ(メタ)アクリレート、ネオペンチルグリコールジ
(メタ)アクリレート、トリメチロールプロパントリ
(メタ)アクリレート、ペンタエリスリトールテトラ
(メタ)アクリレート等の多官能(メタ)アクリレート
モノマーのうち1種または2種以上で置き換えることも
できる。
The acrylic syrup used in the present invention is, for example, methyl (meth) acrylate or ethyl (meth).
1 of alkyl (meth) acrylate monomers such as acrylate, butyl (meth) acrylate, propyl (meth) acrylate, octyl (meth) acrylate, 2-ethylhexyl (meth) acrylate, lauryl (meth) acrylate, stearyl (meth) acrylate Or a mixture of two or more kinds and a polyalkyl (meth) acrylate obtained by using one or more kinds of the above-mentioned monomers as a raw material. In addition, a part of the monomers is ethylene glycol di (meth) acrylate, polyethylene glycol di (meth) acrylate, propylene glycol di (meth) acrylate, neopentyl glycol di (meth) acrylate, trimethylolpropane tri (meth) acrylate, penta. It may be replaced with one or more of polyfunctional (meth) acrylate monomers such as erythritol tetra (meth) acrylate.

【0009】アクリルシロップ中の一官能および多官能
(メタ)アクリレートモノマーと、(メタ)アクリレー
トポリマーの割合は前者が90〜50重量%、後者が1
0〜50重量%で、好ましくは前者が80〜70重量
%、後者が20〜30重量%である。また、多官能(メ
タ)アクリレートモノマーはアクリルシロップ全体の0
〜5重量%、より好ましくは0〜3重量%である。しか
し、多官能モノマーを多量に使用すると樹脂板の軟化温
度が上昇し、また熱時伸張性も低下するため余り深絞り
の成形品には適さない。
The proportion of the monofunctional and polyfunctional (meth) acrylate monomers and the (meth) acrylate polymer in the acrylic syrup is 90 to 50% by weight for the former and 1 for the latter.
0 to 50% by weight, preferably 80 to 70% by weight for the former and 20 to 30% by weight for the latter. Moreover, the polyfunctional (meth) acrylate monomer is 0% of the whole acrylic syrup.
-5% by weight, more preferably 0-3% by weight. However, when a large amount of polyfunctional monomer is used, the softening temperature of the resin plate rises, and the stretchability at the time of heating also decreases, so it is not suitable for a deep-drawn molded product.

【0010】本発明に使用される無機質充填剤は平均粒
径が100μm以下のものであれば良く、例えば、炭酸
カルシウム、タルク、クレー、シリカ、アルミナ、石
英、ケイ酸カルシウム等の金属酸化物の水和物など一般
に用いられているものが使用できる。このような平均粒
径が100μm以下の無機質充填剤の中でもできるだけ
高充填し、且つ低粘度でも安定性良く分散するものが望
ましく、金属酸化物の水和物が特に望ましい。
The inorganic filler used in the present invention may have an average particle size of 100 μm or less. Examples thereof include metal oxides such as calcium carbonate, talc, clay, silica, alumina, quartz and calcium silicate. A commonly used one such as a hydrate can be used. Among such inorganic fillers having an average particle diameter of 100 μm or less, those which are filled as high as possible and are dispersed with good stability even at low viscosity are desirable, and hydrates of metal oxides are particularly desirable.

【0011】アクリルシロップと無機質充填剤とを混練
する際にシランカップリング剤を用いると得られる成形
材料を重合して得た樹脂板の耐水性、耐汚染性、機械強
度が向上するので望ましい。シランカップリング剤とし
ては例えば、γ−メタクリロキシプロピルトリメトキシ
シラン、γ−グリシドキシプロピルトリメトキシシラ
ン、ビニルトリエトキシシラン、ビニルトリアセトキシ
シランなどがある。
When a silane coupling agent is used when kneading the acrylic syrup and the inorganic filler, the resin plate obtained by polymerizing the obtained molding material is improved in water resistance, stain resistance and mechanical strength. Examples of the silane coupling agent include γ-methacryloxypropyltrimethoxysilane, γ-glycidoxypropyltrimethoxysilane, vinyltriethoxysilane, and vinyltriacetoxysilane.

【0012】無機質充填剤の使用量はアクリルシロップ
100重量部に対して20〜200重量部の割合であ
る。20重量部より少ない量では無機質充填剤の沈降が
起こりやすく、また大理石調の美しい外観も得られな
い。また、200重量部を超える量ではアクリルシロッ
プと無機質充填剤の混合物の粘度が高くなりすぎて作業
性が低下する上、得られた樹脂板の剛性が高すぎて加熱
成形できなくなる。更に、樹脂板の透明性も低下して大
理石調の風合いが失われる。
The amount of the inorganic filler used is 20 to 200 parts by weight based on 100 parts by weight of the acrylic syrup. If the amount is less than 20 parts by weight, sedimentation of the inorganic filler easily occurs, and a beautiful marble-like appearance cannot be obtained. If the amount exceeds 200 parts by weight, the viscosity of the mixture of the acrylic syrup and the inorganic filler becomes too high and the workability is deteriorated, and the rigidity of the obtained resin plate is too high to allow thermoforming. Furthermore, the transparency of the resin plate is also reduced, and the texture of marble is lost.

【0013】本発明に使用される重合開始剤としては例
えば、ベンゾイルパーオキサイド、メチルエチルケトン
パーオキサイド等の中温成形で一般に用いられる有機過
酸化物や、それらに組み合わせて使用する促進剤である
有機アミンや多価金属の塩類がある。重合開始剤はアク
リルシロップの重量を基準として0.5〜3%使用する
のが普通である。
Examples of the polymerization initiator used in the present invention include organic peroxides generally used in medium-temperature molding such as benzoyl peroxide and methyl ethyl ketone peroxide, and organic amines which are accelerators used in combination with them. There are salts of polyvalent metals. The polymerization initiator is usually used in an amount of 0.5 to 3% based on the weight of the acrylic syrup.

【0014】アクリルシロップと無機質充填剤を混合
し、重合せしめて得られる樹脂板の作成において、連鎖
移動剤を樹脂配合物中に添加することによってモノマー
成分が重合することによって生成するポリマー成分の分
子量を制御することができる。使用される連鎖移動剤と
しては例えば、α−メチルスチレンダイマーやチオクレ
ゾール、β−メルカプトプロピオン酸オクチル、チオグ
リコール酸オクチル等のメルカプト類等が用いられる。
これらをアクリルシロップの重量を基準として0〜1重
量%添加し、先に述べた重合開始剤を使用することによ
って重量平均分子量20万〜150万のポリマーを得る
ことができる。
In the production of a resin plate obtained by mixing an acrylic syrup and an inorganic filler and polymerizing the mixture, the molecular weight of the polymer component produced by polymerizing the monomer component by adding the chain transfer agent to the resin blend. Can be controlled. Examples of the chain transfer agent used include mercaptos such as α-methylstyrene dimer, thiocresol, octyl β-mercaptopropionate and octyl thioglycolate.
A polymer having a weight average molecular weight of 200,000 to 1,500,000 can be obtained by adding these in an amount of 0 to 1% by weight based on the weight of the acrylic syrup and using the above-mentioned polymerization initiator.

【0015】できたポリマーの分子量が重量平均で20
万未満であると、得られた樹脂板を加熱成形する際に成
形品の肉厚分布が大きくなり、また深絞りの成形品であ
ると高伸張部で破れて成形できなくなる。一方、重量平
均分子量が150万を超えたポリマーでは樹脂板の剛性
が高く、加熱しても軟化しにくく伸張性が低い。従っ
て、生成したポリマーの重量平均分子量20万〜150
万の範囲である必要があり、更に好ましくは50万〜1
00万であることが望まれる。
The resulting polymer has a weight average molecular weight of 20.
If it is less than 10,000, the thickness distribution of the molded product becomes large when the obtained resin plate is heat-molded, and if it is a deep-drawn molded product, it will be broken at the high-stretched portion and cannot be molded. On the other hand, in the case of a polymer having a weight average molecular weight of more than 1,500,000, the resin plate has a high rigidity, is hard to be softened even when heated, and has a low extensibility. Therefore, the weight average molecular weight of the produced polymer is 200,000 to 150.
It should be in the range of 10,000, and more preferably 500,000 to 1
It is desired to be, 000,000.

【0016】また、重合した樹脂板を得るに際し、無機
質充填剤、重合開始剤、シランカップリング剤、連鎖移
動剤以外に必要ならば本発明の効果を阻害しない範囲の
量の各種充填剤、揺変剤、可塑剤、脱泡剤、着色剤など
を加えてもよい。
Further, in obtaining the polymerized resin plate, other than the inorganic filler, the polymerization initiator, the silane coupling agent, and the chain transfer agent, if necessary, various fillers in an amount within the range that does not impair the effect of the present invention, A modifier, a plasticizer, a defoaming agent, a coloring agent and the like may be added.

【0017】更に、重合した樹脂板は厚みが1〜15m
mの範囲に入るように作成する。厚みが1mm未満のも
のであると真空および/または圧空成形において伸張さ
れることによって成形品コーナー部が肉薄となり、さら
には破れることがある。また、厚みが15mmを超える
と真空および/または圧空成形時の樹脂板の伸張応力が
大きくなり、真空や3kgf/cm2程度の圧空では充
分に賦型できなくなる。
Further, the polymerized resin plate has a thickness of 1 to 15 m.
Create so that it falls within the range of m. If the thickness is less than 1 mm, the corner portion of the molded product may become thin and may be broken by being stretched in vacuum and / or pressure molding. On the other hand, if the thickness exceeds 15 mm, the tensile stress of the resin plate during vacuum and / or pressure forming becomes large, and it becomes impossible to sufficiently mold with vacuum or pressure of about 3 kgf / cm 2 .

【0018】本発明を具体的に実施するためには例え
ば、ポリ(メタ)アクリレート10〜50重量部と一官
能(メタ)アクリレートモノマーおよび多官能(メタ)
アクリレートモノマー90〜50重量部からなるアクリ
ルシロップ100重量部に対し、平均粒径100μm以
下の無機質充填剤20〜200重量部、更に重合開始剤
を0.5〜3.0重量部添加して充分に混練分散させ
る。この際、無機質充填剤は予めシランカップリング剤
で処理したものを用いたり、または使用する無機質充填
剤の重量を基準として0.1〜2.0重量%に相当する
シランカップリング剤を前記シロップに溶解ないし分散
させておいてから無機質充填剤を用いることにより、得
られる成形品の耐水性、耐汚染性、機械強度を向上させ
ることができる。更に、重合後生成されるポリマー成分
の分子量を制御するためにアクリルシロップ100重量
部に対して連鎖移動剤を0〜1重量%添加してもよい。
混練方法としては例えば、双腕型ニーダー等の低速混練
機、ディスパー等の高速攪拌機、塗料製造用の顔料分散
機、あるいは混練ロールなどを用いればよく、混練時に
単量体混液中に加える無機質充填剤以外に必要ならば種
々の充填剤、揺変剤、可塑剤、脱泡剤、着色剤などを加
えてもよい。混練して得られた重合前の樹脂配合物の粘
度はポリ(メタ)アクリレート成分の量や充填剤の量に
より異なるが、30℃で数ポイズ〜数千ポイズの範囲に
調節できる。次に得られた樹脂配合物を2枚のステンレ
ス、ガラス等の平板とスペーサーで作成した平板状の型
内に注入して加熱し、(メタ)アクリレートモノマーを
重合させる。肉厚の注型板を重合させる場合は、必要に
応じて水浴など除熱効率のよい媒体中で重合させる。
In order to specifically carry out the present invention, for example, 10 to 50 parts by weight of poly (meth) acrylate, a monofunctional (meth) acrylate monomer and a polyfunctional (meth) acrylate are used.
It is sufficient to add 20 to 200 parts by weight of an inorganic filler having an average particle size of 100 μm or less and 0.5 to 3.0 parts by weight of a polymerization initiator to 100 parts by weight of an acrylic syrup consisting of 90 to 50 parts by weight of an acrylate monomer. Knead and disperse. At this time, as the inorganic filler, one previously treated with a silane coupling agent may be used, or a silane coupling agent corresponding to 0.1 to 2.0% by weight based on the weight of the inorganic filler used may be used as the syrup. By using the inorganic filler after being dissolved or dispersed in, the water resistance, stain resistance and mechanical strength of the obtained molded article can be improved. Furthermore, in order to control the molecular weight of the polymer component produced after the polymerization, a chain transfer agent may be added in an amount of 0 to 1% by weight based on 100 parts by weight of the acrylic syrup.
As a kneading method, for example, a low-speed kneader such as a double-arm kneader, a high-speed agitator such as a disper, a pigment disperser for producing a paint, or a kneading roll may be used, and the inorganic filler added to the monomer mixture during kneading In addition to the agent, various fillers, thixotropic agents, plasticizers, defoamers, coloring agents and the like may be added if necessary. The viscosity of the resin mixture before polymerization obtained by kneading varies depending on the amount of the poly (meth) acrylate component and the amount of the filler, but can be adjusted to a range of several poises to several thousand poises at 30 ° C. Next, the obtained resin composition is poured into a flat plate mold made of two flat plates such as stainless steel and glass and a spacer and heated to polymerize the (meth) acrylate monomer. When a thick cast plate is polymerized, it is polymerized in a medium having a high heat removal efficiency such as a water bath, if necessary.

【0019】このようにして得られた厚み1〜15mm
の樹脂板を加熱器によって樹脂板の軟化点以上、通常1
20〜240℃、に加熱し、その軟化状態の樹脂板を従
来公知の方法で真空および/または圧空成形する。この
時の型の温度は常温でもよいが、樹脂板のガラス転移点
近傍、通常90〜110℃まで加熱し、そこに賦型する
ことによりより肉厚分布の小さな、表面性の優れた成形
品を得ることができる。
The thickness thus obtained is 1 to 15 mm
The resin plate of above is heated by the heater above the softening point of the resin plate, usually 1
It is heated to 20 to 240 ° C., and the resin plate in the softened state is vacuum and / or pressure formed by a conventionally known method. The temperature of the mold at this time may be room temperature, but a molded product having a smaller wall thickness distribution and excellent surface properties by heating to near the glass transition point of the resin plate, usually 90 to 110 ° C., and molding there. Can be obtained.

【0020】[0020]

【実施例】以下、実施例について更に詳細に説明する
が、これらが本発明の全てを代表するものではない。
EXAMPLES Examples will be described in more detail below, but these are not representative of all of the present invention.

【0021】(実施例1)ポリメタクリル酸メチル(ス
ミペックスB−LG−6、住友化学(株)製、以下PM
MAとも記載する。)30重量部をメタクリル酸メチル
70重量部に溶解して100重量部のアクリルシロップ
を得た。得られたアクリルシロップ100重量部に重合
開始剤ベンゾイルパーオキサイドペースト(ナイパーB
O、日本油脂(株)製)2.0重量部、促進剤トリフェ
ニルホスフィン0.5重量部、脱泡剤(BYK A51
5、ビックケミージャパン(株)製)0.1重量部およ
び水酸化アルミニウム(ハイジライトHS−320、昭
和電工(株)製)50重量部を添加し、高速攪拌機を用
いて混練して樹脂配合物を得た。
Example 1 Polymethylmethacrylate (SUMIPEX B-LG-6, manufactured by Sumitomo Chemical Co., Ltd., hereinafter PM)
Also described as MA. ) 30 parts by weight was dissolved in 70 parts by weight of methyl methacrylate to obtain 100 parts by weight of acrylic syrup. 100 parts by weight of the obtained acrylic syrup was added to a polymerization initiator benzoyl peroxide paste (Nyper B
O, 2.0 parts by weight of NOF CORPORATION, 0.5 parts by weight of triphenylphosphine accelerator, defoaming agent (BYK A51)
5, 0.1 parts by weight of Big Chemie Japan Co., Ltd. and 50 parts by weight of aluminum hydroxide (Hijilite HS-320, Showa Denko KK) were added and kneaded with a high-speed stirrer to blend the resin. I got a thing.

【0022】このようにして得た樹脂配合物を2枚のガ
ラス板で厚さ3mmのスペーサーを挟んで作成した型内
に注入し、60℃で100分間加熱して樹脂板を作成し
た。得られた樹脂板のマトリックス樹脂成分の分子量
は、あらかじめ存在していたポリメタクリル酸メチルを
除いて、重量平均で110万、数平均で85万であっ
た。得られた樹脂板を200℃で5分間予備加熱し、排
気口のついた真空または圧空成形用の金型を90℃に保
って、上から3kgf/cm2の圧空をかけて賦型し、
一分間保持して成形品をえた。金型の形状は深さ8c
m、コーナー部の最小半径が5R、平均面積伸張率10
0%(2倍)となる箱型のものを用いた。得られた成形
品はコーナー部まで完全に賦型しており、また肉厚の部
分的バラツキも少なかった。更に、成形品の耐汚染性、
耐熱性も表1に示す通り優れた性能を示した。
The resin composition thus obtained was poured into a mold prepared by sandwiching a spacer having a thickness of 3 mm between two glass plates and heated at 60 ° C. for 100 minutes to prepare a resin plate. The molecular weight of the matrix resin component of the obtained resin plate was 1.1 million on the weight average and 850,000 on the number average, excluding polymethyl methacrylate that was present in advance. The obtained resin plate is preheated at 200 ° C. for 5 minutes, a mold for vacuum or compressed air molding with an exhaust port is maintained at 90 ° C., and a compressed air of 3 kgf / cm 2 is applied from above to mold.
After holding for 1 minute, a molded product was obtained. The shape of the mold is 8c deep
m, minimum radius of corner is 5R, average area expansion rate is 10
A box type of 0% (2 times) was used. The obtained molded product was completely imprinted to the corners, and there was little partial variation in wall thickness. Furthermore, the stain resistance of the molded product,
The heat resistance also showed excellent performance as shown in Table 1.

【0023】(実施例2)実施例1と同様の樹脂配合物
のうち水酸化アルミニウムの添加量のみを100重量部
に変更し、実施例1と同様の方法で樹脂板を製造した。
得られた樹脂板のマトリックス樹脂成分の分子量は、あ
らかじめ存在していたポリメタクリル酸メチル除いて重
量平均で110万、数平均で85万であった。得られた
樹脂板を実施例1と同様の装置、方法で成形して成形品
を得た。得られた成形品はコーナー部まで完全に賦型し
ており、また肉厚の部分的バラツキも小さかった。更
に、成形品の耐汚染性、耐熱性も表1に示す通り優れた
性能を示した。
Example 2 A resin plate was produced in the same manner as in Example 1, except that the amount of aluminum hydroxide added was changed to 100 parts by weight in the same resin composition as in Example 1.
The molecular weight of the matrix resin component of the obtained resin plate was 1,100,000 on the weight average and 850,000 on the number average excluding polymethyl methacrylate which was present in advance. The obtained resin plate was molded by the same apparatus and method as in Example 1 to obtain a molded product. The obtained molded product was completely imprinted to the corners, and the local variation in wall thickness was small. Further, the stain resistance and heat resistance of the molded product also showed excellent performance as shown in Table 1.

【0024】(実施例3)実施例1と同様の樹脂配合お
よび樹脂板製造方法にて厚み10mmの樹脂板を得た。
得られた樹脂板のマトリックス樹脂成分の分子量はあら
かじめ存在していたポリメタクリル酸メチルを除いて、
重量平均で110万、数平均で85万であった。得られ
た樹脂板を200℃で15分間予備加熱し、実施例1と
同様の装置、方法にて成形し、5分間保持して成形品を
得た。得られた成形品はコーナー部まで完全に賦型して
おり、また肉厚の部分的バラツキも小さかった。更に、
成形品の耐汚染性、耐熱性も表1に示す通り優れた性能
を示した。
Example 3 A resin plate having a thickness of 10 mm was obtained by the same resin formulation and resin plate manufacturing method as in Example 1.
The molecular weight of the matrix resin component of the obtained resin plate, except for polymethylmethacrylate that was previously present,
The weight average was 1.1 million and the number average was 850,000. The obtained resin plate was preheated at 200 ° C. for 15 minutes, molded by the same apparatus and method as in Example 1, and held for 5 minutes to obtain a molded product. The obtained molded product was completely imprinted to the corners, and the local variation in wall thickness was small. Furthermore,
The stain resistance and heat resistance of the molded product also showed excellent performance as shown in Table 1.

【0025】(実施例4)アクリルシロップを表1の量
使用する以外は、実施例1と同様の方法で重合して樹脂
板を得た。得られた樹脂板のマトリックス樹脂成分の分
子量は、あらかじめ存在していたポリメタクリル酸メチ
ルを除いて重量平均で140万、数平均で95万であっ
た。得られた樹脂板を実施例1と同様の装置、方法で成
形して成形品を得た。得られた成形品はコーナー部まで
完全に賦型しており、また肉厚の部分的バラツキも小さ
かった。更に、成形品の耐汚染性、耐熱性も表1に示す
通り優れた性能を示した。
Example 4 A resin plate was obtained by polymerization in the same manner as in Example 1 except that the amount of acrylic syrup shown in Table 1 was used. The molecular weight of the matrix resin component of the obtained resin plate was 1.4 million on a weight average and 950,000 on a number average except for polymethylmethacrylate which was present in advance. The obtained resin plate was molded by the same apparatus and method as in Example 1 to obtain a molded product. The obtained molded product was completely imprinted to the corners, and the local variation in wall thickness was small. Further, the stain resistance and heat resistance of the molded product also showed excellent performance as shown in Table 1.

【0026】(実施例5)実施例1と同様の樹脂配合物
に連鎖移動剤としてチオグリコール酸オクチルをアクリ
ルシロップ100重量部に対して0.1重量部添加し、
実施例1と同様の方法で樹脂板を製造した後、120℃
で120分間アフターキュアーした。得られた樹脂板の
マトリックス樹脂成分の分子量は、あらかじめ存在して
いたポリメタクリル酸メチルを除いて重量平均で50
万、数平均で22万であった。得られた樹脂板を実施例
1と同様の装置、方法で成形して成形品を得た。得られ
た成形品はコーナー部まで完全に賦型しており、また肉
厚の部分的バラツキも小さかった。更に、成形品の耐汚
染性、耐熱性も表1に示す通り優れた性能を示した。
Example 5 0.1 part by weight of octyl thioglycolate as a chain transfer agent was added to 100 parts by weight of acrylic syrup in the same resin composition as in Example 1,
After manufacturing a resin plate in the same manner as in Example 1, 120 ° C.
After-curing for 120 minutes. The molecular weight of the matrix resin component of the obtained resin plate was 50 on a weight average basis excluding the preexisting polymethylmethacrylate.
The number average was 220,000. The obtained resin plate was molded by the same apparatus and method as in Example 1 to obtain a molded product. The obtained molded product was completely imprinted to the corners, and the local variation in wall thickness was small. Further, the stain resistance and heat resistance of the molded product also showed excellent performance as shown in Table 1.

【0027】(比較例1)ポリメタクリル酸メチル(ス
ミペックスB―LG―6、PMMAビーズ、住友化学
(株)製)100重量部を200℃に加熱した双腕型ニ
ーダー内で溶融させ、更に水酸化アルミニウム(ハイジ
ライトHS―320、平均粒径3.5μm、昭和電工
(株)製)50重量部を添加、混練した。10分間混練
後、素早く90℃に加温した平板金型上にフィードして
圧縮成形した。用いたポリメタクリル酸メチルの分子量
は重量平均で7万、数平均で3.9万であった。得られ
た厚み3mmの樹脂板を180℃で5分間予備加熱し、
実施例1と同様の装置、方法にて圧空成形したところ、
賦型中に成形品コーナー部が肉薄となり穴があいたため
完全賦型できなかった。
Comparative Example 1 100 parts by weight of polymethylmethacrylate (SUMIPEX B-LG-6, PMMA beads, manufactured by Sumitomo Chemical Co., Ltd.) were melted in a double-arm kneader heated to 200 ° C., and water was further added. 50 parts by weight of aluminum oxide (Hijilite HS-320, average particle size 3.5 μm, manufactured by Showa Denko KK) was added and kneaded. After kneading for 10 minutes, the mixture was rapidly fed to a flat plate mold heated to 90 ° C. and compression-molded. The molecular weight of the polymethylmethacrylate used was 70,000 on a weight average and 39,000 on a number average. The obtained resin plate having a thickness of 3 mm is preheated at 180 ° C. for 5 minutes,
When pressure molding was carried out by the same apparatus and method as in Example 1,
Since the corners of the molded product were thin and had holes during molding, perfect molding was not possible.

【0028】(比較例2)実施例1と同様の樹脂配合物
のうち水酸化アルミニウムの添加量のみを250重量部
に変更し、実施例1と同様の方法で樹脂板を製造した。
得られた樹脂板のマトリックス樹脂成分の分子量は、あ
らかじめ存在していたポリメタクリル酸メチルを除いて
重量平均で110万、数平均で85万であった。得られ
た厚み3mmの樹脂板を実施例1と同様の装置、方法で
成形したところ、賦型中に樹脂板が破れ、成形できなか
った。
Comparative Example 2 A resin plate was manufactured in the same manner as in Example 1, except that the addition amount of aluminum hydroxide was changed to 250 parts by weight in the same resin composition as in Example 1.
The molecular weight of the matrix resin component of the obtained resin plate was 1,100,000 on a weight average and 850,000 on a number average except for polymethylmethacrylate which was present in advance. When the obtained resin plate having a thickness of 3 mm was molded by the same apparatus and method as in Example 1, the resin plate was broken during shaping and could not be molded.

【0029】(比較例3)実施例1と同様の樹脂配合物
を厚み20mmのスペーサーを2枚のガラス板で挟んで
作成した型内に注型し、60℃水浴中で100分間重合
させて樹脂板を得た。得られた樹脂板のマトリックス樹
脂成分の分子量は重量平均で110万、数平均で85万
であった。得られた樹脂板を200℃で15分間予備加
熱し、実施例1と同様の装置、方法で圧空成形を試みた
ところ、樹脂板はわずかに伸張しただけで完全賦型する
にはいたらなかった。更に、同様の樹脂板にて予備加熱
を220℃15分間、圧空圧4kgf/cm2にて成形
を試みたが、これもわずかに伸張しただけで完全賦型す
るに至らなかった。
(Comparative Example 3) The same resin composition as in Example 1 was poured into a mold made by sandwiching a spacer having a thickness of 20 mm between two glass plates and polymerized in a water bath at 60 ° C for 100 minutes. A resin plate was obtained. The weight average molecular weight of the matrix resin component of the obtained resin plate was 1.1 million, and the number average molecular weight was 850,000. The resin plate thus obtained was preheated at 200 ° C. for 15 minutes, and pressure molding was attempted by the same apparatus and method as in Example 1. The resin plate was slightly stretched and could not be completely shaped. . Further, pre-heating was attempted with the same resin plate at 220 ° C. for 15 minutes at a pneumatic pressure of 4 kgf / cm 2 , but this was also slightly stretched but could not be completely shaped.

【0030】(比較例4)アクリルシロップを表1の量
使用する以外は、実施例1と同様の方法で重合して、樹
脂板を得た。得られた樹脂板のマトリックス樹脂成分の
分子量は重量平均で220万、数平均で120万であっ
た。得られた樹脂板を実施例1と同様の装置、方法で成
形したところ、賦型中に樹脂板が破れ、成形できなかっ
た。
Comparative Example 4 A resin plate was obtained by polymerizing in the same manner as in Example 1 except that the amount of acrylic syrup shown in Table 1 was used. The weight average molecular weight of the matrix resin component of the obtained resin plate was 2.2 million, and the number average molecular weight was 1.2 million. When the obtained resin plate was molded by the same apparatus and method as in Example 1, the resin plate broke during shaping and could not be molded.

【0031】[0031]

【表1】 [Table 1]

【0032】[0032]

【表2】 [Table 2]

【0033】[0033]

【発明の効果】本発明は大理石調の美しい外観を持ち、
耐水性、耐熱性、耐汚染性に優れた深絞り成形品を極め
て簡便且つ安価に製造することができる。従って、本発
明方法によって得られる成形品は浴槽、キッチンカウン
ター等、多くの分野で使用できるものである。
The present invention has a beautiful marble-like appearance,
A deep-drawing molded product having excellent water resistance, heat resistance, and stain resistance can be manufactured extremely simply and inexpensively. Therefore, the molded product obtained by the method of the present invention can be used in many fields such as bathtubs and kitchen counters.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 (メタ)アクリル系ポリマーと(メタ)
アクリル系モノマーから成るアクリルシロップ100重
量部に対して、無機質充填剤20〜200重量部および
重合開始剤を混合してなる組成物を重合して重量平均分
子量20万〜150万で、板厚1〜15mmの熱可塑性
樹脂板を成形し、得られた樹脂板を軟化点以上に加熱し
て真空および/または圧空成形することを特徴とする大
理石調成形品の製造方法。
1. A (meth) acrylic polymer and (meth)
A composition in which 20 to 200 parts by weight of an inorganic filler and a polymerization initiator are mixed with 100 parts by weight of an acrylic syrup made of an acrylic monomer is polymerized to have a weight average molecular weight of 200,000 to 1,500,000 and a plate thickness of 1 A method for producing a marble-like molded product, which comprises molding a thermoplastic resin plate having a thickness of up to 15 mm, and heating the obtained resin plate to a softening point or higher for vacuum and / or pressure molding.
JP24793093A 1993-10-04 1993-10-04 Production of marblelike molded product Pending JPH07100908A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP24793093A JPH07100908A (en) 1993-10-04 1993-10-04 Production of marblelike molded product

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP24793093A JPH07100908A (en) 1993-10-04 1993-10-04 Production of marblelike molded product

Publications (1)

Publication Number Publication Date
JPH07100908A true JPH07100908A (en) 1995-04-18

Family

ID=17170673

Family Applications (1)

Application Number Title Priority Date Filing Date
JP24793093A Pending JPH07100908A (en) 1993-10-04 1993-10-04 Production of marblelike molded product

Country Status (1)

Country Link
JP (1) JPH07100908A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010047766A (en) * 2009-10-21 2010-03-04 Mitsubishi Gas Chemical Co Inc Acrylic syrup

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010047766A (en) * 2009-10-21 2010-03-04 Mitsubishi Gas Chemical Co Inc Acrylic syrup

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