JPH083224A - Method for producing methacrylic resin plate for sanitary - Google Patents
Method for producing methacrylic resin plate for sanitaryInfo
- Publication number
- JPH083224A JPH083224A JP6134119A JP13411994A JPH083224A JP H083224 A JPH083224 A JP H083224A JP 6134119 A JP6134119 A JP 6134119A JP 13411994 A JP13411994 A JP 13411994A JP H083224 A JPH083224 A JP H083224A
- Authority
- JP
- Japan
- Prior art keywords
- syrup
- weight
- methacrylic resin
- cell
- methacrylic
- 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.)
- Granted
Links
Landscapes
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
- Bathtubs, Showers, And Their Attachments (AREA)
- Polymerisation Methods In General (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、バスタブや洗面ボウル
等のサニタリー用途に適したアクリル樹脂板の製造方法
に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing an acrylic resin plate suitable for sanitary applications such as bathtubs and washbasins.
【0002】[0002]
【従来の技術】バスタブ、洗面ボウルなどのサニタリー
用品に樹脂製のものが多くなっている。これら樹脂材料
としては、従来不飽和ポリエステルからなるFRPが用
いられることが多かったが、不飽和ポリエステル系材料
は経時的な黄変や傷つき易さ等の欠点を有していること
から、最近では黄変し難く、傷つき難いという特性を有
するメタクリル樹脂系のサニタリー用材料の提案がなさ
れており、一部は実用化されつつある。2. Description of the Related Art Many sanitary products such as bathtubs and washbasins are made of resin. Conventionally, FRP made of unsaturated polyester has often been used as these resin materials, but recently, unsaturated polyester-based materials have drawbacks such as yellowing over time and easy scratching. A methacrylic resin-based material for sanitary products, which has characteristics of being less likely to yellow and less likely to be scratched, has been proposed, and a part thereof is being put to practical use.
【0003】具体的な例を上げると、特開昭54ー60
90号公報には、メタクリル酸メチルに特定の非架橋性
アクリル酸エステル0.2〜8モル%、及び(メタ)ア
クリロイル基を2個以上含む架橋性化合物0.01〜1
モル%を混合したものを重合、固化せしめたメタクリル
樹脂板状成形物の提案がある。又、特開昭60−197
707号公報には、メタクリル酸メチル単独又はメタク
リル酸メチルとアクリル酸エステルとの単量体混合物に
0.01〜2重量%の連鎖移動剤を添加して予備重合し
てシロップを製造し、次いでその得られたシロップに対
して0.02〜1重量%の架橋剤を添加して鋳型中で注
型重合させて熱成形加工性及び耐溶剤性に優れたアクリ
ル樹脂シートの製造方法の提案がある。As a concrete example, Japanese Patent Laid-Open No. 54-60
No. 90 discloses a crosslinkable compound 0.01 to 1 containing 0.2 to 8 mol% of a specific non-crosslinkable acrylic acid ester in methyl methacrylate and two or more (meth) acryloyl groups.
There is a proposal of a methacrylic resin plate-shaped molded product obtained by polymerizing and solidifying a mixture of mol%. In addition, JP-A-60-197
No. 707, 0.01 to 2 wt% of a chain transfer agent is added to methyl methacrylate alone or a monomer mixture of methyl methacrylate and an acrylate ester to carry out prepolymerization to produce a syrup. A proposal of a method for producing an acrylic resin sheet having excellent thermoforming processability and solvent resistance by adding 0.02 to 1% by weight of a crosslinking agent to the obtained syrup and performing cast polymerization in a mold is made. is there.
【0004】[0004]
【発明が解決しようとする課題】特開昭54−6090
号公報に記載の方法で得られるメタクリル樹脂板は、耐
熱、耐溶剤性、接着性等には優れているものの、サニタ
リー用に熱成形するには、その成形性が低い。一方、特
開昭60−197707号公報の方法におけるシロップ
の製造の連鎖移動剤を添加した予備重合反応は、不安定
で、加熱温度や撹拌状態、重合時間などの条件の僅かな
変動で、重合率や分子量の変動が大きく所定分子量、所
定重合率のものを安定的に得ることは容易でなく、特に
重合率の高いシロップを得ようとする場合、その傾向が
一層大きくなる。Problems to be Solved by the Invention JP-A-54-6090
Although the methacrylic resin plate obtained by the method described in JP-A No. 1993-115 is excellent in heat resistance, solvent resistance, adhesiveness, etc., it is low in moldability for thermoforming for sanitary. On the other hand, the prepolymerization reaction in which a chain transfer agent for producing a syrup in the method disclosed in JP-A-60-197707 is added is unstable, and the polymerization is caused by slight fluctuations in conditions such as a heating temperature, a stirring state and a polymerization time. It is not easy to stably obtain a resin having a predetermined molecular weight and a predetermined polymerization rate because of large fluctuations in the rate and the molecular weight, and this tendency becomes even greater when a syrup having a particularly high polymerization rate is to be obtained.
【0005】そこで本発明は、加工性の優れたサニタリ
ー用メタクリル樹脂板を、安定的かつ容易に生産する方
法を提供する。Therefore, the present invention provides a method for stably and easily producing a methacrylic resin plate for sanitary which is excellent in processability.
【0006】[0006]
【課題を解決するための手段】本発明は、メタクリル系
モノマー100重量部に対し、粘度平均分子量 約10
000〜約300000のメタクリル系樹脂5〜50重
量部を溶解させてシロップとし、該シロップをセルに注
入して重合させるサニタリー用メタクリル樹脂板の製造
方法である。According to the present invention, the viscosity average molecular weight is about 10 parts by weight per 100 parts by weight of methacrylic monomer.
It is a method for producing a methacrylic resin plate for sanitary, which comprises dissolving 5 to 50 parts by weight of methacrylic resin of 000 to about 300,000 to form a syrup, and injecting the syrup into a cell to polymerize.
【0007】本発明におけるメタクリル系モノマーと
は、メタクリル酸メチルを主成分とし、必要により共重
合可能なコモノマーを含有するモノマー混合物である。The methacrylic monomer in the present invention is a monomer mixture containing methyl methacrylate as a main component and optionally a copolymerizable comonomer.
【0008】コモノマーの具体例としては、アクリル酸
メチル、アクリル酸エチル、アクリル酸nブチル、アク
リル酸イソブチル、アクリル酸2−エチルヘキシル、ア
クリル酸イソノニル等のアクリル酸アルキルエステル
類;エチレングリコールジメタクリレート、テトラエチ
レングリコールジメタクリレート、ネオペンチルグリコ
ールジメタクリレート、ネオペンチルグリコールジアク
リレート、ヘキサンジオールジメタクリレート、ノナン
ジオールジメタクリレート、トリメチロールプロパント
リメタクリレート、2、2−ビス〔4(メタクリロイル
ポリオキシエチル)フェニル〕プロパン、フタル酸ビス
(2−メタクリロイルオキシエチル)エステル、アリル
メタクリレート、ジビニルベンゼン、ジアリルフタレー
ト等の分子内に2個以上のラジカル重合性基を有する多
官能モノマー類;シクロヘキシルメタクリレート、エチ
ルメタクリレート、フェニルメタクリレート、メタクリ
ル酸、無水マレイン酸、スチレン、シクロヘキシルマレ
イミド、アクリロニトリル等がある。Specific examples of comonomers include alkyl acrylates such as methyl acrylate, ethyl acrylate, n-butyl acrylate, isobutyl acrylate, 2-ethylhexyl acrylate and isononyl acrylate; ethylene glycol dimethacrylate, tetra Ethylene glycol dimethacrylate, neopentyl glycol dimethacrylate, neopentyl glycol diacrylate, hexanediol dimethacrylate, nonanediol dimethacrylate, trimethylolpropane trimethacrylate, 2,2-bis [4 (methacryloylpolyoxyethyl) phenyl] propane, Two in the molecule of phthalic acid bis (2-methacryloyloxyethyl) ester, allyl methacrylate, divinylbenzene, diallyl phthalate, etc. Polyfunctional monomers having a radical polymerizable group above; cyclohexyl methacrylate, ethyl methacrylate, phenyl methacrylate, methacrylic acid, maleic anhydride, styrene, cyclohexyl maleimide, there is acrylonitrile.
【0009】これらのコモノマーは得られる樹脂板の用
途に応じて適宜選択する。この内特に高い成形性が要求
される場合は、上記アクリル酸エステル類をモノマー中
10重量%以内の範囲で用いればよい。また高い耐薬品
性、耐熱性が要求される場合は、分子内に2個以上のラ
ジカル重合性基を有する多官能モノマー類を、モノマー
中0.005〜5重量%の範囲内で用いればよい。These comonomers are appropriately selected depending on the application of the resin plate to be obtained. If particularly high moldability is required, the acrylic ester may be used within the range of 10% by weight in the monomer. When high chemical resistance and heat resistance are required, polyfunctional monomers having two or more radically polymerizable groups in the molecule may be used within the range of 0.005 to 5% by weight in the monomers. .
【0010】本発明においてメタクリル系モノマーに溶
解させるメタクリル系樹脂は、その粘度平均分子量で約
10000〜約300000の範囲内にあるものであ
る。好ましくは粘度平均分子量で50000〜2000
00の範囲であり、更に好ましくは70000〜150
000の範囲である。この範囲の分子量のメタクリル系
樹脂を添加することにより、得られる樹脂板の熱成形時
における加工性を良好にすることができる。粘度平均分
子量が約10000以下のものは、得られる樹脂の加工
性は良好なものの、機械的物性が低いので好ましくな
い。また、粘度平均分子量が約300000を越えるも
のは、加工性が低くなるので好ましくない。In the present invention, the methacrylic resin dissolved in the methacrylic monomer has a viscosity average molecular weight within the range of about 10,000 to about 300,000. The viscosity average molecular weight is preferably 50,000 to 2,000.
00, more preferably 70,000 to 150
The range is 000. By adding a methacrylic resin having a molecular weight in this range, the processability of the obtained resin plate during thermoforming can be improved. When the viscosity average molecular weight is about 10,000 or less, the processability of the obtained resin is good, but the mechanical properties are low, which is not preferable. Further, those having a viscosity average molecular weight of more than about 300,000 are not preferable because the processability becomes low.
【0011】ここでいうメタクリル系樹脂とは、メタク
リル酸メチル単位を主成分としてなる樹脂のことを意味
し、メタクリル酸メチル単独重合体の他、メタクリル酸
メチルとアクリル酸アルキルエステル、スチレン、メタ
クリル酸等のコモノマーとの共重合体も含む。The methacrylic resin as used herein means a resin having a methyl methacrylate unit as a main component, and in addition to methyl methacrylate homopolymer, methyl methacrylate and alkyl acrylate, styrene, methacrylic acid. It also includes a copolymer with a comonomer such as.
【0012】該メタクリル系樹脂の量は、メタクリル系
モノマー混合物100重量部に対し5〜50重量部、好
ましくは10〜40重量部の範囲で用いる。この量が少
ないと、成形性がひくく、多すぎるとシロップの粘度が
高すぎて取り扱いにくくなる。The amount of the methacrylic resin is 5 to 50 parts by weight, preferably 10 to 40 parts by weight, based on 100 parts by weight of the methacrylic monomer mixture. If this amount is too small, the moldability will be poor, and if it is too large, the viscosity of the syrup will be too high and it will be difficult to handle.
【0013】本発明に於いて、シロップとするには、と
にかくメタクリル系モノマーに該メタクリル系樹脂を溶
解させればよくその方法は特定されない。メタクリル系
モノマーに溶解し易くするためメタクリル系樹脂の形態
としては粉末状、ペレット状等、平均サイズ10mm以下
の粒子状の形態として使用するのが好ましい。In the present invention, the syrup may be prepared by dissolving the methacrylic resin in the methacrylic monomer, and the method is not specified. The methacrylic resin is preferably used in the form of powder, pellets or the like in the form of particles having an average size of 10 mm or less so that it can be easily dissolved in the methacrylic monomer.
【0014】このようにして得られるシロップは、保存
安定性も予備重合によって得られるものより優れてい
る。得られたシロップは、溶解時に加熱していた場合に
は室温程度まで冷却する。その後直ちに重合に供するこ
ともできるが、保存安定性が優れているので、室温ない
しそれ以下の温度で保存しておき、必要な時に使用する
こともできる。The syrup thus obtained is also superior in storage stability to that obtained by prepolymerization. If the obtained syrup is heated at the time of dissolution, it is cooled to about room temperature. It can be immediately subjected to polymerization, but since it has excellent storage stability, it can be stored at room temperature or lower and used when necessary.
【0015】重合に供する際、該シロップにラジカル重
合開始剤を添加する。ラジカル重合開始剤は、メタクリ
ル樹脂板の製造に用いられている通常の重合開始剤を用
いることが出来る。例えば、ラウロイルパーオキサイ
ド、ベンゾイルパーオキサイド、ジtブチルパーオキサ
イド、tブチルパーオキシ2エチルヘキサノエート、t
ブチルパーオキシイソブチレート、tブチルパーオキシ
ピバレート、tブチルパーオキシベンゾエート、tブチ
ルパーオキシアセテート、ジイソプロピルパーオキシジ
カーボネート、ジsecブチルパーオキシジカーボネー
ト等の過酸化物系開始剤;2,2’アゾビスイソブチロ
ニトリル、2,2’アゾビス(2,4ージメチルバレロ
ニトリル)等のアゾ系開始剤;更には過酸化物開始剤と
アミン類、メルカプタン類等の還元性化合物を主成分と
して組み合わされた公知のレドックス系開始剤系等を例
示することが出来る。A radical polymerization initiator is added to the syrup when it is subjected to polymerization. As the radical polymerization initiator, a usual polymerization initiator used for producing a methacrylic resin plate can be used. For example, lauroyl peroxide, benzoyl peroxide, di-t-butyl peroxide, t-butyl peroxy 2-ethylhexanoate, t
Peroxide initiators such as butylperoxyisobutyrate, t-butylperoxypivalate, t-butylperoxybenzoate, t-butylperoxyacetate, diisopropylperoxydicarbonate, disec-butylperoxydicarbonate; 2, Azo-based initiators such as 2'azobisisobutyronitrile and 2,2'azobis (2,4-dimethylvaleronitrile); further mainly peroxide initiators and reducing compounds such as amines and mercaptans A known redox type initiator system or the like combined as a component can be exemplified.
【0016】この他に本発明の樹脂の特徴を損なわない
範囲で、用途に応じて公知の添加剤、例えば酸化防止
剤、紫外線吸収剤、連鎖移動剤、離型剤、染料、顔料、
無機系充填剤類等を添加することも可能である。In addition to the above, known additives such as an antioxidant, an ultraviolet absorber, a chain transfer agent, a release agent, a dye, a pigment, etc. may be used depending on the application, as long as the characteristics of the resin of the present invention are not impaired.
It is also possible to add inorganic fillers and the like.
【0017】該シロップを、公知の所謂セルキャスト法
により、セルに注入して重合する。つまり、セルとして
は例えば、2枚のガラス板あるいは金属板と軟質シール
材及びクランプにより構成されたものを用いることが出
来るし、2枚のステンレス製連続ベルトによる連続セル
も使用できる。またセルの厚みは、所望の樹脂板が得ら
れるように選択されるが、一般的には1〜30mmの範囲
である。重合における加熱方法としては公知の方法、例
えば温風、温水、赤外線ヒーター等の熱源によって加熱
する。重合の条件は用いる開始剤の種類や量、また単量
体混合物の組成によって適宜選択されるが、一般的には
50〜120℃で1〜数十時間の範囲で重合を行う。重
合終了後解枠してメタクリル樹脂板を得る。The syrup is injected into a cell and polymerized by a known so-called cell casting method. That is, as the cell, for example, a cell composed of two glass plates or a metal plate, a soft sealing material and a clamp can be used, and a continuous cell using two stainless continuous belts can also be used. The cell thickness is selected so as to obtain a desired resin plate, but is generally in the range of 1 to 30 mm. As a heating method in the polymerization, a known method, for example, hot air, hot water, a heat source such as an infrared heater is used. The polymerization conditions are appropriately selected depending on the type and amount of the initiator used and the composition of the monomer mixture, but generally the polymerization is performed at 50 to 120 ° C. for 1 to several tens of hours. After completion of the polymerization, the frame is opened to obtain a methacrylic resin plate.
【0018】[0018]
【発明の効果】本発明により、サニタリー用メタクリル
樹脂板を安定的かつ容易に生産できる。本発明により得
られる樹脂板は、熱成形時の引っ張り強さが低く、破断
伸び率が大きい為、バスタブ等の深絞りの成形品も容易
に成形することが出来る。つまり、本発明により得られ
る樹脂板は、バスタブ、洗面ボウル等のサニタリー製品
に加工するのに良好な加工性を有している。According to the present invention, a methacrylic resin plate for sanitary can be stably and easily produced. The resin plate obtained by the present invention has a low tensile strength at the time of thermoforming and a large elongation at break, so that a deep-drawn molded product such as a bathtub can be easily molded. That is, the resin plate obtained by the present invention has good workability for processing into sanitary products such as bathtubs and wash bowls.
【0019】[0019]
【実施例】以下、実施例で本発明を具体的に説明する。
尚実施例、比較例における部は、重量部を表す。また、
実施例中において行った物性測定、試験方法は以下の通
りである。 ・粘度平均分子量:ウベローデ粘度計を用いて極限粘度
[η]を求め、次式より粘度平均分子量Mを求めた。 lnM={ln[η]−ln(4.8×10-5)}/
0.8 ・引っ張り試験 :JIS K−7113に準拠してJ
IS2号試験片を用い、試験片を160℃に予熱し、ク
ロスヘッドスピード500mm/分の条件で引っ張り試験
を行い、破断伸び率を求めた。 ・真空成形性:スライド式赤外線ヒータ内蔵の真空成形
装置に底面280mm×280mm、深さ70mm、底面と側
面の境目の辺の曲率半径R=5mmの形状を持つ角形の型
をセットして、表面温度180℃まで加熱してシートを
真空成形し、成型品の辺のRの大小で成形性を評価し
た。 ・FRPによるバッキングテスト:真空成形性テストに
よって得られた成型品の延伸部に、ガラス繊維マットと
不飽和ポリエステル樹脂によりハンドレイアップ法によ
ってバッキングを行い、硬化後の接着面の外観の異常の
有無と密着性を目視で判定した。 ・シロップの保存安定性:シロップを室温で一ヶ月保管
し、変化の有無を調べ、変化の認められないものを○、
著しい粘度上昇もしくは重合固化したものを×とした。EXAMPLES The present invention will be specifically described below with reference to examples.
In addition, the part in an Example and a comparative example represents a weight part. Also,
The physical property measurements and test methods carried out in the examples are as follows. -Viscosity average molecular weight: The intrinsic viscosity [η] was obtained using an Ubbelohde viscometer, and the viscosity average molecular weight M was obtained from the following equation. lnM = {ln [η] -ln (4.8 × 10 -5)} /
0.8 • Tensile test: J according to JIS K-7113
Using the IS2 test piece, the test piece was preheated to 160 ° C., and a tensile test was performed under the condition of a crosshead speed of 500 mm / min to determine the elongation at break.・ Vacuum formability: A square mold with a bottom surface of 280 mm x 280 mm, a depth of 70 mm, and a radius of curvature R = 5 mm at the boundary between the bottom surface and the side surface is set in a vacuum forming device with a slide-type infrared heater, and the surface is set. The sheet was vacuum-formed by heating to a temperature of 180 ° C., and the formability was evaluated by the magnitude of R on the side of the molded product.・ Backing test by FRP: Backing of the molded product obtained by the vacuum moldability test is performed by a hand lay-up method using a glass fiber mat and an unsaturated polyester resin, and the appearance of the adhesive surface after curing is abnormal. And the adhesion was visually determined.・ Storage stability of syrup: Syrup is stored at room temperature for 1 month and checked for changes.
The one in which the viscosity was remarkably increased or the polymerization was solidified was designated as x.
【0020】実施例1 メタクリル酸メチル93.3重量%、2−エチルヘキシ
ルアクリレート6.2重量%、ジアリルフタレート0.
5重量%よりなるモノマーをガラス製容器に入れ、温度
を60℃で撹拌しつつ、懸濁重合法により得られたメタ
クリル酸メチル単位98重量%、メチルアクリレート単
位2重量%、粘度平均分子量約12万の粉末状のメタク
リル系樹脂を、該モノマー100重量部に対し24重量
部添加し、2時間かけて溶解させ、シロップを得た。こ
のシロップは室温で一ヶ月放置後も粘度に変化なく、保
存安定性は○であった。このシロップ100重量部に対
しラジカル重合開始剤として2,2’アゾビスイソブチ
ロニトリル0.1重量%を添加溶解して脱気した後,2
枚のガラス板と塩化ビニール樹脂製ガスケットより構成
された5mm厚のセルに注入し65℃で4時間、その後1
20℃で1時間重合を行った。得られた板の引っ張り試
験による破断伸び率は700%であった。また真空成形
性テストによる辺のRは14mmであった。更に真空性形
性テストによって得られた成型品を用い、FRPによる
バッキングテストを行った結果、外観に異常はなく密着
性も良好であった。Example 1 Methyl methacrylate 93.3% by weight, 2-ethylhexyl acrylate 6.2% by weight, diallyl phthalate 0.
A monomer composed of 5% by weight was placed in a glass container and stirred at a temperature of 60 ° C., and 98% by weight of a methyl methacrylate unit obtained by a suspension polymerization method, 2% by weight of a methyl acrylate unit, a viscosity average molecular weight of about 12 Twenty-five parts of powdery methacrylic resin was added to 24 parts by weight with respect to 100 parts by weight of the monomer and dissolved for 2 hours to obtain a syrup. The syrup showed no change in viscosity even after being left at room temperature for one month, and had a storage stability of O. To 100 parts by weight of this syrup, 0.1% by weight of 2,2'azobisisobutyronitrile as a radical polymerization initiator was added and dissolved, and then degassed.
Inject into a 5 mm thick cell composed of a glass plate and a vinyl chloride resin gasket, and pour at 65 ° C for 4 hours, then 1
Polymerization was carried out at 20 ° C. for 1 hour. The elongation at break in the tensile test of the obtained plate was 700%. Also, the radius R of the side in the vacuum formability test was 14 mm. Furthermore, a molded product obtained by the vacuum formability test was used to perform a backing test by FRP. As a result, the appearance was not abnormal and the adhesion was good.
【0021】実施例2〜4 表1に示す組成のモノマーと、メタクリル系樹脂を用い
た以外は、実施例1と同様に行った。 評価結果を表
2に示す。Examples 2 to 4 The same procedure as in Example 1 was carried out except that a monomer having the composition shown in Table 1 and a methacrylic resin were used. Table 2 shows the evaluation results.
【0022】[0022]
【表1】 [Table 1]
【0023】比較例1 メタクリル酸メチルに、2,2’アゾビスイソブチロニ
トリルを20ppm 添加して70度で予備重合を行い、粘
度平均分子量150万の重合体を5重量%含有するシロ
ップを得た。このシロップ94.5重量部、2エチルヘ
キシルアクリレート5重量部、ジアリルフタレート0.
5重量部及びラジカル重合開始剤としてアゾビスイソブ
チロニトリル0.1重量部を混合溶解し、実施例1と同
様の方法により重合を行った。 得られた板の評価結
果及びシロップの保存安定性を表2に示す。Comparative Example 1 Methyl methacrylate was added with 20 ppm of 2,2′azobisisobutyronitrile and prepolymerized at 70 ° C. to obtain a syrup containing 5% by weight of a polymer having a viscosity average molecular weight of 1,500,000. Obtained. This syrup 94.5 parts by weight, 2 ethylhexyl acrylate 5 parts by weight, diallyl phthalate 0.
5 parts by weight and 0.1 parts by weight of azobisisobutyronitrile as a radical polymerization initiator were mixed and dissolved, and polymerization was carried out by the same method as in Example 1. Table 2 shows the evaluation results of the obtained plate and the storage stability of the syrup.
【0024】比較例2 メタクリル酸メチル96.5重量部、2エチルヘキシル
アクリレート3.5重量部、2,2’アゾビス(2,4
ージメチルバレロニトリル)0.1重量部、ラウリルメ
ルカプタン0.08重量部よりなる混合物を90℃で2
時間予備重合して、重合率25%のシロップを得た。こ
のシロップに含まれる重合体の粘度平均分子量は約8万
であった。このシロップ100重量部に対し、エチレン
グリコールジメタクリレート0.15重量部、2,2’
アゾビスイソブチロニトリル0.1重量部を加え、実施
例と同様の方法により重合を行った。得られた板の評価
結果及びシロップの保存安定性を表2に示す。Comparative Example 2 96.5 parts by weight of methyl methacrylate, 3.5 parts by weight of 2-ethylhexyl acrylate, 2,2'azobis (2,4
-Dimethylvaleronitrile) 0.1 part by weight and lauryl mercaptan 0.08 part by weight at 90 ° C for 2 hours.
Prepolymerization was carried out for a time to obtain a syrup having a polymerization rate of 25%. The viscosity average molecular weight of the polymer contained in this syrup was about 80,000. To 100 parts by weight of this syrup, 0.15 parts by weight of ethylene glycol dimethacrylate, 2,2 '
0.1 part by weight of azobisisobutyronitrile was added, and polymerization was carried out in the same manner as in Example. Table 2 shows the evaluation results of the obtained plate and the storage stability of the syrup.
【0025】比較例3 メタクリル酸メチルに対し、2,2’アゾビスイソブチ
ロニトリルを20ppm添加して70度で予備重合を行
い、粘度平均分子量150万の重合体を5重量%含有す
るシロップを得た。このシロップ100重量部、及びラ
ジカル重合開始剤として2,2’アゾビスイソブチロニ
トリル0.1重量部を混合溶解し、実施例1と同様の方
法により重合を行った。 得られた板の評価結果及びシ
ロップの保存安定性を表2に示す。Comparative Example 3 Syrup containing 5% by weight of a polymer having a viscosity average molecular weight of 1,500,000 by adding 20 ppm of 2,2′azobisisobutyronitrile to methyl methacrylate and prepolymerizing at 70 ° C. Got 100 parts by weight of this syrup and 0.1 parts by weight of 2,2′azobisisobutyronitrile as a radical polymerization initiator were mixed and dissolved, and polymerization was carried out by the same method as in Example 1. Table 2 shows the evaluation results of the obtained plate and the storage stability of the syrup.
【0026】[0026]
【表2】 [Table 2]
Claims (1)
し、粘度平均分子量約10000〜約300000のメ
タクリル系樹脂5〜50重量部を溶解させてシロップと
し、該シロップをセルに注入して重合させるサニタリー
用メタクリル樹脂板の製造方法。1. A sanitary product in which 5 to 50 parts by weight of a methacrylic resin having a viscosity average molecular weight of about 10,000 to about 300,000 is dissolved in 100 parts by weight of a methacrylic monomer to prepare a syrup, and the syrup is injected into a cell for polymerization. Method for producing methacrylic resin plate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13411994A JP3460307B2 (en) | 1994-06-16 | 1994-06-16 | Method for producing methacrylic resin plate for sanitary |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13411994A JP3460307B2 (en) | 1994-06-16 | 1994-06-16 | Method for producing methacrylic resin plate for sanitary |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH083224A true JPH083224A (en) | 1996-01-09 |
| JP3460307B2 JP3460307B2 (en) | 2003-10-27 |
Family
ID=15120912
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP13411994A Expired - Fee Related JP3460307B2 (en) | 1994-06-16 | 1994-06-16 | Method for producing methacrylic resin plate for sanitary |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3460307B2 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2797634A1 (en) * | 1999-08-20 | 2001-02-23 | Sumitomo Chemical Co | Resin panel for use in manufacture of sanitary ware, has high break elongation and low flow and relaxation indices |
| JP2017529445A (en) * | 2014-09-29 | 2017-10-05 | エルジー・ケム・リミテッド | Acrylic syrup manufacturing method and acrylic syrup |
-
1994
- 1994-06-16 JP JP13411994A patent/JP3460307B2/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2797634A1 (en) * | 1999-08-20 | 2001-02-23 | Sumitomo Chemical Co | Resin panel for use in manufacture of sanitary ware, has high break elongation and low flow and relaxation indices |
| AU773365B2 (en) * | 1999-08-20 | 2004-05-20 | Sumitomo Chemical Company, Limited | Methacrylic resin board used for producing sanitary goods and process for producing said board |
| JP2017529445A (en) * | 2014-09-29 | 2017-10-05 | エルジー・ケム・リミテッド | Acrylic syrup manufacturing method and acrylic syrup |
| US10131728B2 (en) | 2014-09-29 | 2018-11-20 | Lg Chem, Ltd. | Acrylic syrup preparation method and acrylic syrup |
Also Published As
| Publication number | Publication date |
|---|---|
| JP3460307B2 (en) | 2003-10-27 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| RU2400500C9 (en) | Use of granular polyalkyl(meth)acrylate polymers and moulding compound for making extrusion moulded articles with dull surface | |
| JPH0151497B2 (en) | ||
| GB2089354A (en) | Polymerization of methyl methacrylate | |
| JP3695239B2 (en) | Manufacturing method of sanitary methacrylic resin plate | |
| JPS61162509A (en) | Thermoplastic resin and thermoplastic resin composition containing the same | |
| JP3460307B2 (en) | Method for producing methacrylic resin plate for sanitary | |
| JPH0219843B2 (en) | ||
| JP3061551B2 (en) | Method for producing methacrylic resin | |
| JPS61151212A (en) | Methacrylate copolymer and its production | |
| JP3557732B2 (en) | Method for manufacturing acrylic resin plate | |
| AU773365B2 (en) | Methacrylic resin board used for producing sanitary goods and process for producing said board | |
| JP7713305B2 (en) | Methacrylic resin casting plate | |
| JP3508251B2 (en) | Method for producing methacrylic resin cast plate | |
| JPS60144308A (en) | Method for manufacturing impact-resistant methacrylic resin sheet | |
| JPH08301937A (en) | Method for producing methacrylic polymer | |
| JPH06322035A (en) | Acrylic resin plate for sanitary | |
| JP2001131296A (en) | Methacrylic resin plate for manufacturing sanitary products and method for manufacturing the resin plate | |
| JP3882247B2 (en) | Acrylic artificial marble and method for producing the same | |
| JPH09174676A (en) | Acrylic product manufacturing method | |
| JPS60245661A (en) | Organic-inorganic composite composition | |
| JP2547003B2 (en) | Method for producing high refractive index copolymer | |
| JPH04227613A (en) | Production of methacrylic resin excellent in heat-resistance, colorlessness and transparency | |
| JP3615875B2 (en) | Methacrylic resin casting polymer | |
| JP2024137773A (en) | Resin Molding | |
| JP3440781B2 (en) | Resin composition, artificial marble obtained by molding the same, and method for producing the same |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| S531 | Written request for registration of change of domicile |
Free format text: JAPANESE INTERMEDIATE CODE: R313531 |
|
| S533 | Written request for registration of change of name |
Free format text: JAPANESE INTERMEDIATE CODE: R313533 |
|
| R350 | Written notification of registration of transfer |
Free format text: JAPANESE INTERMEDIATE CODE: R350 |
|
| FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20070815 Year of fee payment: 4 |
|
| FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20080815 Year of fee payment: 5 |
|
| FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20080815 Year of fee payment: 5 |
|
| RD05 | Notification of revocation of power of attorney |
Free format text: JAPANESE INTERMEDIATE CODE: R3D05 |
|
| FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20090815 Year of fee payment: 6 |
|
| LAPS | Cancellation because of no payment of annual fees |