JPH0453860A - Methacrylate resin composition - Google Patents
Methacrylate resin compositionInfo
- Publication number
- JPH0453860A JPH0453860A JP15980090A JP15980090A JPH0453860A JP H0453860 A JPH0453860 A JP H0453860A JP 15980090 A JP15980090 A JP 15980090A JP 15980090 A JP15980090 A JP 15980090A JP H0453860 A JPH0453860 A JP H0453860A
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- Prior art keywords
- polymerization
- resin composition
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- ppm
- molding
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Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、メタクリル酸メチル系共重合体と特定量、か
つ特定組成のグリセリン高級脂肪族モノエステルとから
なる射出成形時の離型性に優れ、かつ成形品の外観の良
好なメタクリル系樹脂組成物に関する。[Detailed Description of the Invention] [Field of Industrial Application] The present invention provides a method for improving mold releasability during injection molding, which is composed of a methyl methacrylate copolymer and a specific amount and composition of a glycerin higher aliphatic monoester. The present invention relates to a methacrylic resin composition that is excellent and gives molded products a good appearance.
従来、メタクリル系樹脂組成物の成形においては、離型
に対して特に工業的実施上支障となるような問題は起こ
っていなかったため積極的な離型処方を行う必要はなか
ったし、また金型などに塗布するいわゆる外部離型剤も
成形品の美観を損なうおそれがあるために通常は用いら
れていなかった。Conventionally, in the molding of methacrylic resin compositions, there was no need for active mold release formulations because there were no problems with mold release that would hinder industrial implementation. So-called external mold release agents, which are applied to molded parts, have not usually been used because they may impair the aesthetic appearance of molded products.
しかしながら近年、メタクリル系樹脂成形におけるロボ
ント化の導入によって樹脂成形加工の途中において、成
形品が機械的に取り扱われるようになってきたため良離
型性付与技術は生産性向上に対する有力な手段の一つと
なりうること、光学レンズや光ディスクのような超鏡面
金型成形においては、成形品と金型面との密着性が極め
て高くなるために長蛇型性の樹脂が要求されていること
、あるいは、光学レンズのような高精度の表面を有する
成形品を得るために超高圧射出成形機による成形が行わ
れているが、この際金型からの離型が比較的困難となる
ために長蛇型性材料が必要であること、等の観点から、
優れた離型性を有するメタクリル系樹脂成形材料の要求
が高まってきた。However, in recent years, with the introduction of robotization in methacrylic resin molding, molded products have come to be handled mechanically during the resin molding process, so technology that provides good mold release properties is one of the effective means for improving productivity. In the case of ultra-mirror mold molding for optical lenses and optical discs, long-shaped resin is required to achieve extremely high adhesion between the molded product and the mold surface. In order to obtain molded products with high-precision surfaces, such as lenses, molding is performed using ultra-high pressure injection molding machines, but in this case, it is relatively difficult to release the mold from the mold, so long-forming materials are used. From the perspective of the need for
There has been an increasing demand for methacrylic resin molding materials with excellent mold release properties.
従来、離型剤として用いられていたものには流動パラフ
ィン、ワックス、高級脂肪酸及びそのエステル、高級脂
肪族アルコール等が知られていた。Conventionally, liquid paraffin, wax, higher fatty acids and their esters, higher aliphatic alcohols, etc. have been known as mold release agents.
しかしながら、これらの添加剤を懸濁法等のスラリー重
合系に用いようとすると酸系のものは重合系を著しく不
安定にし、また中性のものも一定量以上添加することが
できずにさらに、離型性は期待していたほどに向上しな
かった。また、重合時の助則と離型剤等その他の添加剤
とを配合して用いるので外観が一層劣悪になることも大
きな問題であった。However, when trying to use these additives in a slurry polymerization system such as a suspension method, acidic additives make the polymerization system extremely unstable, and neutral additives cannot be added in excess of a certain amount. However, the mold releasability did not improve as much as expected. Another major problem was that the external appearance deteriorated because the polymerization aids and other additives such as a mold release agent were used in combination.
メタクリル酸メチル系共重合体を注型重合する際に、離
型剤として多価アルコール、脂肪酸エステル、脂肪酸(
及びアミ1)、脂肪族金属塩等を単量体中に混合して重
合生成物を得る方法が開示されている(特開昭61−7
3754)。しかしながらこの方法では、満足な離型効
果を得るための離型剤濃度が1000〜20000 p
pmと高いために熱変形温度の低下を招くなど好ましく
ない物性変動をきたす。When casting methyl methacrylate copolymer, polyhydric alcohols, fatty acid esters, fatty acids (
and Ami 1), a method of obtaining a polymerization product by mixing an aliphatic metal salt, etc. into a monomer is disclosed (Japanese Patent Application Laid-Open No. 61-7
3754). However, in this method, the concentration of the mold release agent to obtain a satisfactory mold release effect is 1000 to 20000 p.
pm, which causes undesirable changes in physical properties such as a decrease in heat distortion temperature.
更に、この方法では得られるメタクリル系樹脂成形体の
種類が限定されるので射出成形品の離型性改良には必ず
しも寄与していない。Furthermore, since this method limits the types of methacrylic resin moldings that can be obtained, it does not necessarily contribute to improving the mold releasability of injection molded products.
また、ステアリン酸やステアリン酸金属塩などの高級脂
肪酸及びその金属塩は離型効果が良好なことで知られて
いるが、金属面を著しく腐蝕させることが重大な問題と
なっていた。Furthermore, higher fatty acids such as stearic acid and metal stearate and their metal salts are known to have good mold release effects, but they have caused a serious problem in that they significantly corrode metal surfaces.
さらにメタクリル系樹脂成形品の離型性改良を目的とし
て、メタクリル酸メチル系共重合体を注型重合によって
得る際に注型用鋳型の形状を工夫することによって注型
成形時の離型性を改良する方法が開示されている。(時
開61−222708、時開6l−222709)、
Lかしながらこのような改良は極めて特殊な成形品を得
る方法に限定されることがら、離型性の本質的改良が達
成されたとはいいがたがった。Furthermore, with the aim of improving the releasability of methacrylic resin molded products, we improved the mold releasability during cast molding by devising the shape of the casting mold when obtaining methyl methacrylate copolymer by cast polymerization. A method of improvement is disclosed. (Opening hours 61-222708, opening hours 6l-222709),
However, since such improvements are limited to methods for obtaining extremely specific molded products, it has been difficult to claim that a substantial improvement in mold releasability has been achieved.
また、射出成形時の離型性を改良する方向として、グリ
セリン高級脂肪酸エステル及び飽和脂肪族高級アルコー
ルを添加する方法が開示されている(特開平1−294
763)、 Lかしながら、この方法でも離型性の改良
がまだ十分ではな(、さらに射出成形品の表面に銀条痕
が発生ずる場合も認められた。Additionally, a method of adding glycerin higher fatty acid esters and saturated aliphatic higher alcohols has been disclosed in order to improve mold releasability during injection molding (JP-A-1-294
However, even with this method, the improvement in mold releasability was still insufficient (furthermore, it was observed that silver streaks appeared on the surface of the injection molded product in some cases).
本発明者らは、以上のような従来の離型性付与処方の欠
点を克服し、射出成形時の離型性が著しく改良され、か
つ、成形品の表面の銀条痕発生が抑制され、さらに従来
の物と比較して機械強度、耐熱性などの点で遜色のない
メタクリル系樹脂組成物を見出し、本発明に至った。The present inventors have overcome the drawbacks of the conventional mold release property imparting formulations as described above, and the mold release property during injection molding is significantly improved, and the generation of silver streaks on the surface of the molded product is suppressed. Furthermore, the inventors have discovered a methacrylic resin composition that is comparable in mechanical strength, heat resistance, etc. to conventional products, leading to the present invention.
即ち、本発明は、メタクリル酸メチル系共重合体と、下
記一般式(1)にて表されるグリセリン高級脂肪酸モノ
エステル500ppm〜5000ppmとからなるメタ
クリル系樹脂組成物に関するものであり、C11−0−
と−R
さH−0−H(1)
昌2−O−H
R4:炭素数が10〜30であるアルキルで、かつ、炭
素数18であるアルキルの比率が80〜99%であるア
ルキル
さらにステアリルアルコールを500〜3000ppm
含有する上記記載のメタクリル樹脂組成物に関するもの
である。That is, the present invention relates to a methacrylic resin composition comprising a methyl methacrylate copolymer and 500 ppm to 5000 ppm of a glycerin higher fatty acid monoester represented by the following general formula (1), and relates to a C11-0 −
and -R SaH-0-H (1) 昌2-O-H R4: Alkyl having 10 to 30 carbon atoms, and an alkyl in which the ratio of alkyl having 18 carbon atoms is 80 to 99%; 500-3000ppm stearyl alcohol
The present invention relates to the above-mentioned methacrylic resin composition containing the above-mentioned methacrylic resin composition.
本発明の樹脂組成物の成分であるグリセリン高級脂肪酸
モノエステルは、下記一般式(1)で表わされるが、
昌2−〇−H
R1:炭素数が10〜30であるアルキルで、かつ、炭
素数18であるアルキルの比率が80〜99%であるア
ルキル
R1において、炭素数18であるアルキルの比率が80
〜99%であることが重要である。この比率が80%未
満では、離型性に劣るだけでなく、成形品の表面に銀条
痕が発生しやすくなる。一方、この比率が99%を超え
る場合には、金型表面にくもりが生じやすく、その為、
成形品表面にくもりが転写されるという問題がある。ま
た、この比率が99%を超えるグリセリン高級脂肪酸モ
ノエステルは、工業的に生産されていない。仮に、この
ものを製造したとしても価格が非常に高いため汎用樹脂
の添加剤としてはコストデメリントが大である。好まし
い比率は85〜99%である。The glycerin higher fatty acid monoester, which is a component of the resin composition of the present invention, is represented by the following general formula (1), where R1: alkyl having 10 to 30 carbon atoms; In alkyl R1 where the ratio of alkyl having number 18 is 80 to 99%, the ratio of alkyl having carbon number 18 is 80%
It is important that it be ~99%. If this ratio is less than 80%, not only the mold releasability is poor, but also silver streaks are likely to occur on the surface of the molded product. On the other hand, if this ratio exceeds 99%, clouding tends to occur on the mold surface, and therefore,
There is a problem that cloudiness is transferred to the surface of the molded product. Moreover, glycerin higher fatty acid monoesters with this ratio exceeding 99% are not produced industrially. Even if this product were to be manufactured, it would be very expensive and would have a significant cost disadvantage as an additive for general-purpose resins. The preferred ratio is 85-99%.
炭素数18であるアルキルの比率が80〜99%の場合
に、このように著しい離型性改良効果、銀条痕抑制効果
及び成形品のくもり抑制効果を示す理由は明らかではな
いが、アルキルの炭素数が変化することにより、グリセ
リン高級脂肪酸モノエステルの極性が変化し、その結果
、メタクリル系共重合体との相溶性が変化することに一
因があると推定される。It is not clear why when the ratio of alkyl having 18 carbon atoms is 80 to 99%, the effect of improving mold releasability, suppressing silver streaks, and suppressing clouding of molded products is so remarkable. It is presumed that one reason is that the polarity of the glycerin higher fatty acid monoester changes due to the change in the number of carbon atoms, and as a result, the compatibility with the methacrylic copolymer changes.
また含有量は500〜5000ppmの範囲であり、好
ましくは700〜3000ppmである。この含有量が
500 ppm未満である場合には、離型効果が著しく
低下し、5000ppmを超えて使用された場合には樹
脂組成物の離型性は良好であるが耐熱変形性が低下し、
かつ樹脂からの添加剤のブリードによる金型面の汚染が
はなはなだしい。Moreover, the content is in the range of 500 to 5000 ppm, preferably 700 to 3000 ppm. When this content is less than 500 ppm, the mold release effect is significantly reduced, and when it is used in excess of 5000 ppm, the mold release property of the resin composition is good, but the heat deformation resistance is reduced.
In addition, the mold surface is severely contaminated due to bleeding of additives from the resin.
一般に、工業的に生産されているグリセリン高級脂肪酸
モノエステルには、ジエステル、トリエステルが不純物
として数パーセント含有されるが、この程度の量であれ
ば、本発明の組成物の特徴を損なうことはない。Generally, industrially produced glycerin higher fatty acid monoester contains several percent of diesters and triesters as impurities, but this amount will not impair the characteristics of the composition of the present invention. do not have.
また、ステアリルアルコールを500〜3000 pp
m含有する本発明の組成物は、離型性、成形品外観に優
れるという特徴を維持した上に成形加工性が良好となる
。この量が500ppm未満の場合には、成形加工性の
改善効果が現われず、3000ppmを超える場合には
耐熱変形性の低下を招き好ましくない。好ましくは75
0〜2000ppmである。In addition, 500 to 3000 pp of stearyl alcohol
The composition of the present invention containing m maintains the characteristics of excellent mold releasability and molded product appearance, and also has good molding processability. If this amount is less than 500 ppm, no effect of improving molding processability will appear, and if it exceeds 3000 ppm, heat deformation resistance will deteriorate, which is undesirable. Preferably 75
It is 0 to 2000 ppm.
本発明の組成物におけるメタクリル酸メチル系共重合体
とは、メタクリル酸メチル単位を主単位とし、これと共
重合しうるモノマー単位とからなる共重合体をいう。メ
タクリル酸メチル単位は、70重量%以上あるものが好
ましい。共重合しうるモノマー単位として、例えば、ア
クリル酸メチル単位、アクリル酸エチル単位、アクリル
酸ブチル単位、アクリル酸イソブチル単位、アクリル酸
2−エチルヘキシル単位、メタクリル酸シクロヘキシル
単位、メタクリル酸し−ブチルシクロヘキシル単位が好
ましい。これらのモノマー単位は共重合体中、0.5重
量%以上30重量%未満あるものが好ましい。0.5重
量%未満では、成形時の熱分解挙動が激しく、30重量
%以上では耐熱変形性の著しい低下等を招くので、好ま
しくない。重量平均分子量は、5万〜50万がよく、好
ましくは5万〜30万、より好ましくは6万〜20万で
ある。The methyl methacrylate copolymer in the composition of the present invention refers to a copolymer consisting of a methyl methacrylate unit as a main unit and a monomer unit copolymerizable with the methyl methacrylate unit. The content of methyl methacrylate units is preferably 70% by weight or more. Examples of copolymerizable monomer units include methyl acrylate units, ethyl acrylate units, butyl acrylate units, isobutyl acrylate units, 2-ethylhexyl acrylate units, cyclohexyl methacrylate units, and butylcyclohexyl methacrylate units. preferable. The content of these monomer units in the copolymer is preferably 0.5% by weight or more and less than 30% by weight. If it is less than 0.5% by weight, the thermal decomposition behavior during molding will be severe, and if it is more than 30% by weight, it will cause a significant decrease in heat deformation resistance, which is not preferable. The weight average molecular weight is preferably 50,000 to 500,000, preferably 50,000 to 300,000, more preferably 60,000 to 200,000.
メタクリル酸メチル系共重合体の製造方法は、キャスト
重合、塊状重合、懸濁重合、溶液重合、乳化重合等の一
般の行われている重合方法によって製造することができ
る。溶液重合を行う場合には、単量体混合物をトルエン
、エチルベンゼン等の芳香族炭化水素の溶媒に溶解して
調製した溶液を用いることができる。懸濁重合や乳化重
合により重合させる場合には、媒体として水を用いて行
うことができる。塊状重合により重合させる場合には、
通常行われるように加熱により生じる遊離ラジカルや電
離性放射線照射により重合を開始させることができる。The methyl methacrylate copolymer can be produced by commonly used polymerization methods such as cast polymerization, bulk polymerization, suspension polymerization, solution polymerization, and emulsion polymerization. When performing solution polymerization, a solution prepared by dissolving a monomer mixture in an aromatic hydrocarbon solvent such as toluene or ethylbenzene can be used. When polymerizing by suspension polymerization or emulsion polymerization, water can be used as a medium. When polymerizing by bulk polymerization,
Polymerization can be initiated by free radicals generated by heating or by irradiation with ionizing radiation, as is commonly done.
本発明の共重合体の重合反応に用いられる開始剤として
は、一般にラジカル重合において用いられる任意の開始
剤を使用することができ、例えばアブビスイソブチルニ
トリル等のアゾ化合物、ヘンシイルバーオキサイド、ラ
ウロイルパーオキサイド、tert−ブチルパーオキシ
−2−エチルヘキサノエート等の有機過酸化物が用いら
れ、又特に90°C以上の高温下で重合を行わせる場合
には、溶液重合が一般的であるので、10時間半減期温
度が80°C以トでかつ用いる有機溶媒に可)容である
過酸化物、アゾビス開始剤等が好ましく、具体的には1
,1−ビス(t−ブチルパーオキシ)33゜5−トリメ
チルシクロヘキサン、シクロヘキサノンバーオキシト、
2,5〜ジメチル−2,5−ジ(−。As the initiator used in the polymerization reaction of the copolymer of the present invention, any initiator generally used in radical polymerization can be used, such as azo compounds such as abbis isobutyl nitrile, hensyl peroxide, lauroyl Organic peroxides such as peroxide and tert-butylperoxy-2-ethylhexanoate are used, and especially when polymerization is carried out at a high temperature of 90°C or higher, solution polymerization is common. Therefore, peroxides, azobis initiators, etc. whose 10-hour half-life temperature is 80°C or higher and are compatible with the organic solvent used are preferred.
, 1-bis(t-butylperoxy)33゜5-trimethylcyclohexane, cyclohexanone peroxide,
2,5-dimethyl-2,5-di(-.
ン゛ゾイルバーオキン)ヘキサン、1,1−アゾビス(
1−シクロヘキサンカルボニトリル)、2(カルバモイ
ルアン゛ンイソフ゛チロニトリル等ヲ挙げることができ
る。これらの開始剤は0.005〜5重量%の範囲で用
いられる。本発明の共重合体の重合反応に必要Qこ応し
て用いられる分子量調節剤は、−船釣なラジカル重合に
おいて用いる任意のものが使用され、例えばブチルメル
カプタン、オクチルカプタン、ドデシルメルカプタン、
チオグリコール酸2−エチルヘキシル等のメルカプタン
化合物が特に好ましいものとして挙げられる。これらの
分子M調節剤は、共重合体の重合度が上記の範囲内に制
御されるような濃度範囲で添加される。hexane, 1,1-azobis(
Examples include 1-cyclohexanecarbonitrile), 2-(carbamoyl anionisobutyronitrile), etc. These initiators are used in a range of 0.005 to 5% by weight.Polymerization of the copolymer of the present invention Q required for the reaction The molecular weight regulator used accordingly is any one used in radical polymerization, such as butyl mercaptan, octyl captan, dodecyl mercaptan,
Particularly preferred are mercaptan compounds such as 2-ethylhexyl thioglycolate. These molecular M regulators are added in a concentration range such that the degree of polymerization of the copolymer is controlled within the above range.
本発明の組成物におけるグリセリニア・・高級脂肪酸モ
ノエステルの添加方法としては、千ツマ−に熔解し7て
均一溶液として重合する方法と、熔融状態、ヒース状、
或いはベレット状の共重合体に後添加(7て混練する方
法がある。グリセリン高級脂肪酸モノエステルの効果を
有効に発現させる為乙こは後添加方法が望ましい。この
原因については明確ではないが、グリセリン高級脂肪酸
モノエステルの分散状態、化学的変質などが関与してい
ると推定される。Methods for adding glycerinia higher fatty acid monoester to the composition of the present invention include a method in which it is dissolved in 1,000 pieces and then polymerized as a homogeneous solution;
Alternatively, there is a method of post-adding (7) kneading to a pellet-shaped copolymer.In order to effectively express the effect of glycerin higher fatty acid monoester, the post-adding method is preferable.The reason for this is not clear, but It is presumed that the dispersion state of glycerin higher fatty acid monoester, chemical alteration, etc. are involved.
また、本発明の組成物には、その特性を損わない範囲で
公知の添加剤、例えば、滑剤、酸化防止剤5.帯電防止
剤、紫外線吸収剤等を添加することができる。In addition, the composition of the present invention may contain known additives such as lubricants, antioxidants, etc., to the extent that their properties are not impaired. Antistatic agents, ultraviolet absorbers, etc. can be added.
(実施例)
共重合体及びその組成物の各種分析及び物性評価は以下
の方法によった。(Example) Various analyzes and physical property evaluations of copolymers and compositions thereof were performed by the following methods.
(1)共重合体中のモノマー単位
分解炉温度450°Cでの熱分解ガスクロマトグラフィ
ー法により、各構成単位庖定量した。(1) Monomer unit decomposition in copolymer Each constituent unit was quantified by pyrolysis gas chromatography at a furnace temperature of 450°C.
(2)重量平均分子量
共重合体の重量平均分子量はゲルパーミエイションクロ
マトグラフィ−(GPC)測定によった。GPC測定は
、共重合体を一定量テトラヒドロフランに溶解させて(
30■/30d )試料溶液を調整して測定したものを
標準ポリス千しノから得られた検量線をもとにPMMA
に換算して値を得た。(2) Weight average molecular weight The weight average molecular weight of the copolymer was measured by gel permeation chromatography (GPC). GPC measurement is performed by dissolving a certain amount of the copolymer in tetrahydrofuran (
30■/30d) Prepare the sample solution and measure it using PMMA based on the calibration curve obtained from the standard polychishino.
The value was obtained by converting it into .
(3)グリセリン高級脂肪酸モノエステルの定量樹脂組
成物をアセトンに一定量溶解した後メタノールでポリマ
ー分を再沈させる。ポリマを濾別後溶液を蒸発乾固した
ものをピリジンを溶媒としてBAS (ビストリメチル
シリルアセトアミド)と反応させて得られたものに一定
量の内部標準物質を添加してG C,分析を行った。(3) Quantification of Glycerin Higher Fatty Acid Monoester After dissolving a certain amount of the resin composition in acetone, the polymer component is reprecipitated with methanol. After the polymer was filtered off, the solution was evaporated to dryness and reacted with BAS (bistrimethylsilylacetamide) using pyridine as a solvent. A certain amount of an internal standard substance was added to the resulting product, followed by GC and analysis.
(4)加熱変形温度(l(DT)
ASTM−0648にもとづいて測定を行った。試験片
は96°Cで2時間アニーリングを行った後挟L!調節
(23°C1相対湿度52%で48時間)を行って測定
した。(4) Heating distortion temperature (l(DT)) Measurement was carried out based on ASTM-0648.The test piece was annealed at 96°C for 2 hours, and then adjusted to 48°C at 23°C and 52% relative humidity. time).
(5)成形性(MFI)
AST?I 01238の■法(230°C13,8k
g)で、M F I (g/10 min )を測定し
た。(5) Moldability (MFI) AST? Method ■ of I 01238 (230°C13,8k
g), MFI (g/10 min) was measured.
(6)M型性評価
3oz射出成形機に第1図に示すような4段プレート型
の金型を取りつけ、成形温度250 ’(1、金型温度
50°C及び射出圧力920 kg/crAの条件下で
成形を行ったとき、4段プレー ト成形中にヒビ、カケ
、ワレが発生したものを不良品と見なし、全成形品中の
不良品の割合を不良発生率として定義した。(6) Evaluation of M-type property A 4-stage plate mold as shown in Figure 1 was attached to a 3oz injection molding machine, and the molding temperature was 250' (1. The mold temperature was 50°C and the injection pressure was 920 kg/crA. When molding was performed under these conditions, products that developed cracks, chips, or cracks during four-stage plate molding were considered to be defective products, and the percentage of defective products among all molded products was defined as the defect incidence rate.
サンプル総数は、射出成形条件を一定にするために20
shot成形した後、1005hot成形を行った。従
って、総数−100で評価した。The total number of samples was 20 to keep the injection molding conditions constant.
After shot molding, 1005 hot molding was performed. Therefore, the total number was evaluated as -100.
なお、成形にあたっては、ペレノトを乾燥し、水分率0
.06重量%以下で使用した。In addition, when molding, Perenoto is dried and the moisture content is 0.
.. It was used in an amount of 0.6% by weight or less.
(7)銀条痕評価
離型性評価を行った同じ成形品において、表面に銀条痕
が認められるものを不良品と見なし、全成形品中の不良
品の割合を不良発生率とじて定義した。(7) Silver streak evaluation Among the same molded products that were subjected to mold releasability evaluation, those with silver streaks observed on the surface are considered to be defective products, and the percentage of defective products in all molded products is defined as the defective incidence rate. did.
(8)金型表面くもり評価
(6)、(7)評価用の成形品を成形した後の金型の表
面を目視で観察し、そのくもりの程度をランク付けした
。(8) Evaluation of mold surface cloudiness (6), (7) After molding the molded product for evaluation, the surface of the mold was visually observed, and the degree of cloudiness was ranked.
◎ くもりなし
○ くもりほとんどなし
△ くもりあり
× 著しいくもり
実施例1
内容1t13ffのガラス製セパラブルフラスコに、純
水5700 g懸濁安定剤として第3リン酸カルシウム
28.5 g 、、ラウリル硫酸ナトリウム0.23
gを分散させた後、メタクリル酸メチル3705 g、
アクリル酸メチル95g、7ヅビスイソブチロニ[・リ
ル5.7g 、及びn−オクチルメルカプタン9.9g
からなる混合溶液を加え、攪拌下80°Cで重合を行っ
た。◎ No cloudiness ○ Almost no cloudiness △ Cloudy × Significant cloudiness Example 1 Contents: 5700 g of pure water in a 1 ton, 13 ff glass separable flask, 28.5 g of tribasic calcium phosphate as a suspension stabilizer, 0.23 g of sodium lauryl sulfate.
After dispersing g, 3705 g of methyl methacrylate,
95 g of methyl acrylate, 5.7 g of 7-bisisobutyroni[-ril, and 9.9 g of n-octyl mercaptan.
A mixed solution consisting of was added, and polymerization was carried out at 80°C with stirring.
次いで重合系を室温まで冷却して内容物を濾過、水洗浄
、乾燥することによって無色のビーズ状重合体を得た。Next, the polymerization system was cooled to room temperature, and the contents were filtered, washed with water, and dried to obtain a colorless bead-like polymer.
得られたビーズ状重合体は、スクリュー径30閣φのヘ
ント型2軸押出機を用いて押出しを行ったが、この際、
ビーズ状重合体に対してR6において、炭素数18であ
るアルキルの比率が85%である高級脂肪酸モノグリセ
リ1−及びステアリルアルコール各々1000 ppm
ずつ配合して押出しを行った。The obtained bead-like polymer was extruded using a Ghent-type twin-screw extruder with a screw diameter of 30 mm.
1000 ppm each of higher fatty acid monoglyceride 1- and stearyl alcohol in which the ratio of alkyl having 18 carbon atoms is 85% in R6 to the bead-like polymer
Each was blended and extruded.
ここに得られた樹脂組成物は、ペレット状になっており
、これを先に説明した方法で一般的な物性及び離型性の
評価を行った。これらの結果を第1表及び第2表に示す
。The resin composition obtained here was in the form of pellets, and its general physical properties and mold release properties were evaluated using the methods described above. These results are shown in Tables 1 and 2.
実施例2〜6、比較例1〜5
ステアリルアルコール及び高級脂肪酸モノグリセリドの
組成及び添加量を変更した以外は実施例1と同様に行っ
た。結果を第1表及び第2表に示す。Examples 2 to 6, Comparative Examples 1 to 5 The same procedure as in Example 1 was carried out except that the composition and addition amount of stearyl alcohol and higher fatty acid monoglyceride were changed. The results are shown in Tables 1 and 2.
実施例7
メタクリル酸メナル68重量%、アクリル酸メチル2重
量%、エチルヘンゼア30重量%、Llシタ シャリ−
ブチルパーオキし/3.3.5−)リメチルシクロヘキ
サン300ppm及びn−オクチルメルカプタン800
ppmからなる混合溶液を総容量101の密封式圧力容
器に連続的に供給し、平均温度100°C1滞留時間1
20分で重合を行わせた後重合反応槽側に接続された貯
槽で減圧することによって揮発成分を除去した後に、連
続的に押出機に溶融状態で移送される。ここで、押出機
に接続している添加剤投入口からステアリルアルコル1
000 ppm及びR1において、炭素数18であるア
ルキルの比率が85%である高級脂肪酸モノグリセリド
1000 ppwl を90゛Cでン容融した4大態で
定量的にフィードして樹脂組成物をベレットの状態で得
た。得られたペレット状の樹脂組成物は、実施例1と同
様の評価方法を実施した。これらの結果を第1表及び第
2表に示す。Example 7 Menal methacrylate 68% by weight, methyl acrylate 2% by weight, ethylhenzea 30% by weight, Ll.
Butyl peroxidation/3.3.5-)limethylcyclohexane 300 ppm and n-octyl mercaptan 800
A mixed solution consisting of
After polymerization was carried out for 20 minutes, the volatile components were removed by reducing the pressure in a storage tank connected to the polymerization reaction tank, and then the mixture was continuously transferred in a molten state to an extruder. Here, stearyl alcohol 1 is added from the additive inlet connected to the extruder.
000 ppm and R1, 1000 ppwl of higher fatty acid monoglyceride in which the proportion of alkyl having 18 carbon atoms is 85% was dissolved at 90°C and quantitatively fed in four forms to form the resin composition into pellets. I got it from The obtained pellet-shaped resin composition was subjected to the same evaluation method as in Example 1. These results are shown in Tables 1 and 2.
実施例8
実施例1において単量体をメタクリル酸メチル3050
g、アクリル酸メチル150g、メタクリル酸t−ブ
チルシクロヘキシル600gに変更した以外は実施例1
と全く同様に行った。Example 8 In Example 1, the monomer was methyl methacrylate 3050
Example 1, except that 150 g of methyl acrylate and 600 g of t-butylcyclohexyl methacrylate were used.
I did exactly the same thing.
結果を第1表及び第2表6ご示す。The results are shown in Table 1 and Table 2.6.
以下余白
モノマ
第
表
単(!7(iitり
グリセリン殉樹盟1省エステル
* MMA : メタクリル酸メチル
*MA ・アクリル酸メチル
* t−BCMMA・ メタクリル酸t−フチルンク
ロヘキノル(発明の効果〕
本発明によれば、射出成形時の離型性が著しく改良され
、かつ、成形品の表面の銀条痕発生が抑制され、さらに
従来の物と比較して機械強度、耐熱性などの点で遜色の
ないメタクリル系樹脂組成物を得ることができる。Below is a blank monomer table (!7 (iit glycerin martyrdom tree alliance 1 saving ester) * MMA: Methyl methacrylate * MA ・Methyl acrylate * t-BCMMA ・ t-phthyl methacrylate Chlorohexynol (Effects of the invention) According to the present invention, the mold releasability during injection molding is significantly improved, the occurrence of silver streaks on the surface of the molded product is suppressed, and the mechanical strength, heat resistance, etc. are improved compared to conventional products. A comparable methacrylic resin composition can be obtained.
第1図は離型性評価の説明図である。 特許出願人 旭化成工業株式会社 完今1ill堅 a−5しL Nh、こしし FIG. 1 is an explanatory diagram of mold releasability evaluation. Patent applicant: Asahi Kasei Industries, Ltd. Complete now 1ill solid a-5 L Nh, Koshishi
Claims (1)
)にて表されるグリセリン高級脂肪酸モノエステル50
0ppm〜5000ppmとからなるメタクリル系樹脂
組成物。 ▲数式、化学式、表等があります▼(1) R_1:炭素数が10〜30であるアルキルで、かつ、
炭素数18であるアルキルの比率が80〜99%である
アルキル 2、ステアリルアルコールを500〜3000ppm含
有する特許請求の範囲第1項に記載のメタクリル系樹脂
組成物。[Claims] 1. Methyl methacrylate copolymer and the following general formula (1
) Glycerin higher fatty acid monoester 50
A methacrylic resin composition comprising 0 ppm to 5000 ppm. ▲There are mathematical formulas, chemical formulas, tables, etc.▼ (1) R_1: Alkyl having 10 to 30 carbon atoms, and
The methacrylic resin composition according to claim 1, which contains alkyl 2 having a carbon number of 18 in a ratio of 80 to 99%, and stearyl alcohol in an amount of 500 to 3000 ppm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15980090A JPH0453860A (en) | 1990-06-20 | 1990-06-20 | Methacrylate resin composition |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15980090A JPH0453860A (en) | 1990-06-20 | 1990-06-20 | Methacrylate resin composition |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0453860A true JPH0453860A (en) | 1992-02-21 |
Family
ID=15701536
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP15980090A Pending JPH0453860A (en) | 1990-06-20 | 1990-06-20 | Methacrylate resin composition |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0453860A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2279351A (en) * | 1993-05-31 | 1995-01-04 | Kuraray Co | Methacrylic resin composition |
| WO2015041311A1 (en) * | 2013-09-20 | 2015-03-26 | 株式会社クラレ | Resin composition and molded article thereof |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH01294763A (en) * | 1988-05-23 | 1989-11-28 | Asahi Chem Ind Co Ltd | Methacrylic resin composition |
-
1990
- 1990-06-20 JP JP15980090A patent/JPH0453860A/en active Pending
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH01294763A (en) * | 1988-05-23 | 1989-11-28 | Asahi Chem Ind Co Ltd | Methacrylic resin composition |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2279351A (en) * | 1993-05-31 | 1995-01-04 | Kuraray Co | Methacrylic resin composition |
| US5510408A (en) * | 1993-05-31 | 1996-04-23 | Kuraray Co., Ltd. | Methacrylic resin composition and method for production thereof |
| GB2279351B (en) * | 1993-05-31 | 1997-01-08 | Kuraray Co | Methacrylic resin composition and method for production thereof |
| CN1076742C (en) * | 1993-05-31 | 2001-12-26 | 可乐丽股份有限公司 | Methacrylic resin composition and method for production thereof |
| WO2015041311A1 (en) * | 2013-09-20 | 2015-03-26 | 株式会社クラレ | Resin composition and molded article thereof |
| CN105555863A (en) * | 2013-09-20 | 2016-05-04 | 株式会社可乐丽 | Resin composition and molded article thereof |
| JPWO2015041311A1 (en) * | 2013-09-20 | 2017-03-02 | 株式会社クラレ | Resin composition and molded product thereof |
| TWI651333B (en) * | 2013-09-20 | 2019-02-21 | 可樂麗股份有限公司 | Resin composition and molded article thereof |
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