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JPS6257487B2 - - Google Patents
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JPS6257487B2 - - Google Patents

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Publication number
JPS6257487B2
JPS6257487B2 JP13965780A JP13965780A JPS6257487B2 JP S6257487 B2 JPS6257487 B2 JP S6257487B2 JP 13965780 A JP13965780 A JP 13965780A JP 13965780 A JP13965780 A JP 13965780A JP S6257487 B2 JPS6257487 B2 JP S6257487B2
Authority
JP
Japan
Prior art keywords
injection
satin
resin
molded product
mold
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
Application number
JP13965780A
Other languages
Japanese (ja)
Other versions
JPS5763353A (en
Inventor
Naoyuki Suzuki
Tomohiko Yoshida
Shinichi Ikeda
Juichi Myahara
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.)
Mitsubishi Chemical Corp
Original Assignee
Mitsubishi Rayon 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 Mitsubishi Rayon Co Ltd filed Critical Mitsubishi Rayon Co Ltd
Priority to JP13965780A priority Critical patent/JPS5763353A/en
Publication of JPS5763353A publication Critical patent/JPS5763353A/en
Publication of JPS6257487B2 publication Critical patent/JPS6257487B2/ja
Granted legal-status Critical Current

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  • Moulds For Moulding Plastics Or The Like (AREA)
  • Injection Moulding Of Plastics Or The Like (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は陽極皮膜処理を施された梨地アルミニ
ウム様の表面光沢を有するポリエステル製射出成
形品に関する。 陽極皮膜処理を施された梨地アルミニウム成形
品は表面光沢に深みがあり優美な艶を有し、これ
まで化粧品瓶のキヤツプ、コンパクト、高級万年
筆、飾り皿等の高級品イメージを要求される分野
に広く用いられている。ところでこれら梨地アル
ミニウム成形品の製造方法としてはまずアルミニ
ウム材を所望の形状に冷間加工等で作成し、バリ
取りを行なつた後サンドプラスト等で梨地加工を
行ない、より洗浄した後脱脂、水洗し、必要に応
じて電解研摩や化学研摩を施し、次いで陽極皮膜
処理を施し、さらには着色処理を施す方法が行な
われている。この際成形品に高級イメージを与え
るために陽極皮膜を厚くする必要があり、その結
果長時間の陽極皮膜処理が必要となる。しかるに
このような種々の煩雑な製造工程と長時間の電気
的処理を施すためかかる成形品の製造コストは非
常に高価なものとなつている。従つて化粧品容器
等の高付加価値を有する成形品であつてもその製
造コストが問題になり、より安価で容易に得られ
る陽極皮膜処理を施された梨地アルミニウム様外
観を有する成形品の開発が強く望まれていた。 本発明者らはかかる現状に鑑み上記陽極皮膜処
理を施された梨地アルミニウム成形品に酷似した
外観を有するプラスチツク成形品を安価にかつ容
易に得るべく鋭意検討した結果特定範囲量のポリ
エステル系樹脂と特定範囲量のポリオレフイン系
樹脂及びメタクリル系樹脂とからなる群から選ば
れた少なくとも一種とを配合した樹脂組成物を用
い、これを金型内面が梨地加工された梨地様表面
を有する射出成形金型により成形された射出成形
品が上記目的を満足しうることを見出し本発明に
到達した。 即ち本発明の要旨とするところは、固有粘度が
0.6以上のポリエステル系樹脂60〜99.5重量%と
ポリオレフイン系樹脂及びメタクリル系樹脂とか
らなる群から選ばれた少なくとも一種40〜0.5重
量%とからなる樹脂組成物から構成され、金型内
面が梨地加工された射出成形金型により成形され
たポリエステル製射出成形品にある。 本発明におけるポリエステル系樹脂とはそれを
構成するくり返し単位の60モル%以上がエチレン
テレフタレートからなるものであり共重合体も含
まれる。共重合成分としてはイソフタル酸、アジ
ピン酸、セバシン酸、P−β−オキシエトキシ安
息香酸、ジフエニルエーテル−4・4′−ジカルボ
ン酸、ジフエノキシエタン−4・4′−ジカルボン
酸等またはこれらのアルキルエステル誘導体等の
ジカルボン酸成分、プロピレングリコール、ブタ
ンジオール、ヘキサメチレングリコール、ネオペ
ンチルグリコール、シクロヘキサンジメタノール
等のグリコール類が用いられる。ポリエステル系
樹脂はエステル交換反応を経て重縮合を行なう方
法、あるいは直接エステル化を経て重縮合を行な
う方法、さらにはこれらの方法によつて得られた
ポリマーを固相重合する方法のいずれの方法によ
つて得られるポリマーを使用することができるが
その固有粘度〔η〕は0.6以上、好ましくは0.65
〜1.4の範囲であることが望ましい。〔η〕が0.6
未満の場合には最終的に得られる成形品の外観が
損われ目的とする深みのある優美な表面光沢が発
現しなくなるので好ましくない。一方〔η〕が高
すぎる場合、例えば1.4を超えるものでは樹脂の
溶融粘度が高くなりその射出成形性が悪くなるた
め好ましくない。なお〔η〕はフエノール/テト
ラクロルエタン=50/50(重量比)溶液中25℃で
測定した溶液粘度より求めた値である。 また本発明におけるポリオレフイン系樹脂とは
エチレン、プロピレン、ブテン−1・4−メチル
ペンテン−1、イソブチレン等の単独重合体また
はこれらα−オレフインを主成分とする他のコモ
ノマーとの共重合体というものである。共重合体
の具体例としてはエチレン−酢酸ビニル共重合
体、エチレン−アクリル酸共重合体、エチレン−
アクリル酸メチル共重合体、エチレン−プロピレ
ン共重合体等が挙げられる。本発明の実施に際し
てはエチレン−酢酸ビニル共重合体、エチレン−
アクリル酸メチル共重合体体、ポリプロピレン等
が優れた効果を発揮し特に好ましいものである。 さらに本発明におけるメタクリル系樹脂とはメ
タクリル酸メチルの単独重合体、50モル%以上の
メタクリル酸メチルと他のビニル単量体との共重
合体をいう。メタクリル酸メチルと共重合せしめ
る他のビニル単量体としてはアクリル酸メチル、
アクリル酸エチル、アクリル酸ブチル等のアクリ
ル酸アルキルエステル類、メタクリル酸エチル、
メタクリル酸ブチル等のメタクリル酸アルキルエ
ステル類、アクリロニトリル、メタクリロニトリ
ル、スチレン、α−メチルスチレン等が挙げられ
る。本発明の実施に際してはメタクリル酸メチル
の単独重合体あるいはアクリル酸メチルやアクリ
ル酸エチルとの共重合体を使用する場合特に優れ
た効果が得られ好ましいものである。 本発明の実施に際しては上記ポリオレフイン系
樹脂及びメタクリル系樹脂は夫々単独で、または
ポリオレフイン系樹脂同志あるいはメタクリル系
樹脂同志を併用して、さらにはポリオレフイン系
樹脂の少なくとも一種とメタクリル系樹脂の少な
くとも一種とを併用してポリエステル系樹脂に混
合して用いることができるがその配合量は上記ポ
リエステル系樹脂が60〜99.5重量%、ポリオレフ
イン系樹脂及びメタクリル系樹脂とからなる群か
ら選ばれた少なくとも一種が40〜0.5重量%の範
囲であることが必要である。本発明の射出成形品
を構成する上記樹脂組成物が上記範囲を逸脱した
場合にはこれを後述する特定の梨地加工された射
出成形金型によつて成形しても本発明の特徴であ
る陽極皮膜処理を施された梨地アルミニウム様の
表面光沢が発現しにくくなるので好ましくない。
即ち上記樹脂組成物中のポリエステル系樹脂の含
有量が99.5重量%を超える場合には最終的に得ら
れる射出成形品の透明感が強くなり曇り硝子状と
なる。一方ポリエステル系樹脂の含有量が60重量
%未満の場合には深みのある優美な艶のある光沢
が発現せず素焼陶器様の外観となつたりするなど
目的とする表面光沢が得にくい上、エチルアルコ
ール、香料等に長時間さらされるとクラツクが発
生しやすく、また強度の低下も大きいため好まし
くない。 本発明において上記ポリエステル系樹脂にポリ
オレフイン系樹脂及びメタクリル系樹脂の少なく
とも一種を混合する方法は適宜の方法を用いうる
が上記夫々の樹脂粉末、ペレツトをミキサーで混
合した後溶融押出機によりペレツト化する方法が
好適である。この際該押出機のスクリユー先端に
混練効果を高めるためにミキシングゾーンを設け
たり、例えばL/Dが20以上で且つ圧縮比が2.0
以上のスクリユーを用いたり、二軸スクリユーを
用いることにより良好な外観が得られ好ましいも
のである。 次に本発明の射出成形品は上記特定の樹脂組成
物を金型内面が梨地加工された射出成形金型によ
り成形されるわけであるがその際に使用する金型
内面はその目的とする外観パターンに応じて金型
製品部表面の一部又は全部が梨地加工されていれ
ばよい。これら金型内面の梨地加工は腐食加工、
放電加工等により行なうことができる。この金型
内面の梨地模様の表面粗さは目的とする成形品の
外観に応じて選択しうるが具体例としては例えば
宮森金属製作所製シボ加工サンプル番号で挙げれ
ばB39D、B39CD、B39C、B39BC、B39B、
B39AB、B684、B9A等が好適なものであるが勿
論これに限定されるものではない。 本発明を実施するに際しては射出成形機は一般
に用いられている機種をいずれも用い得るがスク
リユー形状や射出成形条件によつて成形品の表面
光沢の度合は影響を受ける傾向にある。従つてス
クリユーは圧縮ゾーン及びメタリングゾーンが
夫々少なくとも3ピツチを有し、圧縮比が1.5〜
4のものが好適である。また射出成形条件で重要
なことは射出速度と金型温度である。射出速度が
大になるに従い深みのある表面光沢が得られるた
め好ましいものである。しかし射出速度を極端に
大きくするとゲート周辺部の表面光沢が消失した
り、汚れが発生したりする上強い流れ模様が発現
し上品さがなくなる傾向にあり適度の射出速度が
要求される。一方金型温度は50℃以下に設定され
ていることが好ましく、これより温度が高い場合
には射出成形品の冷却固化に長時間を要し成形サ
イクルが長くなり、またこのような状態で成形す
ると成形品の結晶が起こり、本発明の目的とする
陽極皮膜処理を施された深みのある梨地アルミニ
ウム様表面光沢が得られなくなるので好ましくな
い。 本発明の射出成形品は上述した如き特定量の樹
脂から構成される樹脂組成物を射出成形すること
によつて成形品表面にパール状表面光沢を発現せ
しめると共に金型内面に形成された梨地模様を射
出成形時に成形品表面に付与せしめることの相乗
作用により初めて得られるものであり、成形品表
面の梨地表面下のパール状表面光沢を与える樹脂
層の存在が本発明の特徴である深みのある梨地ア
ルミニウム様表面光沢外観を与えるものと考えら
れる。 本発明においては本発明の目的を逸脱しない範
囲で染顔料、紫外線吸収剤、帯電防止剤、核剤等
の添加物を加えても構わない。 本発明の射出成形品は上述した如き陽極皮膜処
理を施された梨地アルミニウム様の美麗な深みの
ある表面光沢を有し、且つアルコール類、香料、
弱酸等に対する耐薬品性に優れ、衝撃強度、曲げ
強度等の機械的強度、保香性、衛生性等に優れて
いることから化粧品や医薬品の容器のキヤツプ、
コンパクト類、口紅容器、万年筆の軸胴部、電気
器具のつまみ等に好ましく用いることができる。 以下実施例により本発明を具体的に説明する。 実施例1〜5、比較例1〜2 水分率50ppm以下とされた〔η〕が0.9のポリ
エチレンテレフタレート(以後PETと略記す
る。)のペレツトに25℃のクロロホルム中で測定
した〔η〕(dl/g)が0.6のメタクリル酸メチ
ル/アクリル酸メチル=90/10(重量比)の組成
を有するメタクリル系共重合体のペレツトを85℃
で20時間乾燥した後第1表に示す割合になるよう
に配合したものをL/D=24、供給ゾーン11D、
圧縮ゾーン6D、メタリングゾーン7D、ピツチ
1D、圧縮比2.5のスクリユーを具備した東芝機械
製40mmφ押出機に供給し押出成形して平均3φ×
3mmの寸法を有するペレツトを得た。この際シリ
ンダー温度は後部260℃、中部270℃、前部280
℃、ダイ280℃、スクリユー回転数60rpmの条件
で行なつた。得られたペレツト中のポリエチレン
テレフタレートの〔η〕の測定値は0.83〜0.87の
範囲であつた。これらペレツトをベースにして10
倍濃度にした青色のマスターバツチを夫々賦形
し、これらマスターバツチ10重量部と上記混合樹
脂組成ペレツト90重量部とを混合し、150℃にて
5時間真空乾燥した後にL/D=17、供給ゾーン
8.5D、圧縮ゾーン5.3D、メタリングゾーン
3.2D、ピツチ0.9D、圧縮比3.0のスクリユーを具
備した名機製作所SJ−40C射出成形機により、そ
の内面が宮森金属製作所シボ加工サンプル番号
B39Cの梨地加工された同時に2個成形できるサ
イドゲートでコールドランナー方式の金型を用い
て重量15g、平板の半分の肉厚が3mm、残り半分
の肉厚が1.5mmの段付きの片面が梨地加工された
50×100mmの平板を成形した。成形条件は次の通
りであつた。シリンダー温度はC1270℃、C2280
℃、C3290℃、ノズル290℃、射出一次圧(ゲー
ジ圧)30Kg/cm2、射出二次圧(ゲージ圧)20Kg/
cm2、射出スピード50g/秒、成形サイクル30秒、
金型温度10℃であつた。 得られた成形品は表面外観と40℃1ケ月エタノ
ール浸漬テストによる外観変化とについて評価を
行なつた。これらの結果を各平板中のPETの
〔η〕と共に第1表に示す。 なお第1表中の外観評価の表示は次の通りであ
る(これらの表示法は以後の実施例、比較例に共
通である)。 ◎:陽極皮膜処理を施された梨地アルミニウムの
表面光沢と同等の表面光沢を有するもの 〇:陽極皮膜処理を施された梨地アルミニウムの
表面光沢にかなり近い表面光沢を有するもの △:陽極皮膜処理を施された梨地アルミニウムの
表面光沢にかなり近い表面光沢は認められるが
その状態が弱いもの ×:透明感が強かつたり又は素焼陶器様であり当
該梨地アルミニウム表面光沢に全く似ていない
もの
The present invention relates to an injection molded polyester product that has been subjected to an anodic coating treatment and has a surface gloss similar to that of matte aluminum. Satin aluminum molded products treated with anodic coating have a deep and elegant surface gloss, and have been used in fields that require a high-class image such as cosmetic bottle caps, compacts, luxury fountain pens, and decorative plates. Widely used. By the way, the method for producing these matte aluminum molded products is to first create the aluminum material into the desired shape by cold working, remove burrs, perform a satin finish using sandplast, etc., and then clean it, degrease it, and wash it with water. However, if necessary, electrolytic polishing or chemical polishing is performed, followed by an anodic coating treatment, and furthermore, a coloring treatment is performed. At this time, it is necessary to thicken the anodic coating in order to give the molded product a high-class image, and as a result, a long period of anodic coating treatment is required. However, due to the various complicated manufacturing steps and long-time electrical processing, the manufacturing cost of such molded products is extremely high. Therefore, even for molded products with high added value such as cosmetic containers, the manufacturing cost becomes an issue, and it is difficult to develop molded products that are cheaper and easier to obtain and have a satin aluminum appearance that has been subjected to an anodic coating treatment. It was strongly desired. In view of the current situation, the inventors of the present invention conducted intensive studies to easily obtain a plastic molded product having an appearance similar to the matte aluminum molded product subjected to the anodic coating treatment at a low cost. An injection mold having a satin-like surface in which the inner surface of the mold is treated with a satin-like surface using a resin composition blended with at least one selected from the group consisting of a polyolefin resin and a methacrylic resin in a specific range amount. The inventors have discovered that an injection molded article formed by the method can satisfy the above object, and have arrived at the present invention. That is, the gist of the present invention is that the intrinsic viscosity is
It is composed of a resin composition consisting of 60 to 99.5% by weight of a polyester resin of 0.6 or higher and 40 to 0.5% by weight of at least one type selected from the group consisting of polyolefin resins and methacrylic resins, and the inner surface of the mold has a satin finish. This is a polyester injection molded product molded using a molded injection mold. The polyester resin used in the present invention is one in which 60 mol% or more of the repeating units constituting the resin consists of ethylene terephthalate, and also includes copolymers. Copolymerization components include isophthalic acid, adipic acid, sebacic acid, P-β-oxyethoxybenzoic acid, diphenyl ether-4,4'-dicarboxylic acid, diphenoxyethane-4,4'-dicarboxylic acid, etc. Dicarboxylic acid components such as alkyl ester derivatives of , glycols such as propylene glycol, butanediol, hexamethylene glycol, neopentyl glycol, and cyclohexanedimethanol are used. Polyester resins can be produced by any of the following methods: polycondensation via transesterification, direct esterification and polycondensation, or solid phase polymerization of the polymers obtained by these methods. The resulting polymer can be used, but its intrinsic viscosity [η] is 0.6 or more, preferably 0.65.
A range of ~1.4 is desirable. [η] is 0.6
If it is less than that, the appearance of the final molded product will be impaired and the desired deep and elegant surface gloss will not be developed, which is not preferable. On the other hand, if [η] is too high, for example exceeding 1.4, the melt viscosity of the resin will increase and its injection moldability will deteriorate, which is not preferable. Note that [η] is a value determined from the solution viscosity measured at 25°C in a phenol/tetrachloroethane=50/50 (weight ratio) solution. Furthermore, the polyolefin resin in the present invention refers to a homopolymer of ethylene, propylene, butene-1,4-methylpentene-1, isobutylene, etc., or a copolymer containing these α-olefins as a main component with other comonomers. It is. Specific examples of copolymers include ethylene-vinyl acetate copolymer, ethylene-acrylic acid copolymer, and ethylene-vinyl acetate copolymer.
Examples include methyl acrylate copolymer and ethylene-propylene copolymer. When carrying out the present invention, ethylene-vinyl acetate copolymer, ethylene-vinyl acetate copolymer, ethylene-vinyl acetate copolymer,
Methyl acrylate copolymers, polypropylene, etc. exhibit excellent effects and are particularly preferred. Furthermore, the methacrylic resin in the present invention refers to a homopolymer of methyl methacrylate or a copolymer of 50 mol% or more of methyl methacrylate and another vinyl monomer. Other vinyl monomers that can be copolymerized with methyl methacrylate include methyl acrylate,
Acrylic acid alkyl esters such as ethyl acrylate and butyl acrylate, ethyl methacrylate,
Examples include methacrylic acid alkyl esters such as butyl methacrylate, acrylonitrile, methacrylonitrile, styrene, α-methylstyrene, and the like. In carrying out the present invention, it is preferable to use a homopolymer of methyl methacrylate or a copolymer with methyl acrylate or ethyl acrylate because particularly excellent effects can be obtained. In carrying out the present invention, the above-mentioned polyolefin resin and methacrylic resin may be used alone, or in combination with polyolefin resins or methacrylic resins, or in combination with at least one polyolefin resin and at least one methacrylic resin. It can be used in combination with the polyester resin in an amount of 60 to 99.5% by weight of the above polyester resin and 40% by weight of at least one selected from the group consisting of polyolefin resin and methacrylic resin. It is necessary that the content be in the range of ~0.5% by weight. If the resin composition constituting the injection molded article of the present invention deviates from the above range, it may be molded using a specific satin-finished injection mold described later. This is not preferable because it becomes difficult to develop a surface gloss similar to that of matte aluminum that has been subjected to film treatment.
That is, when the content of the polyester resin in the resin composition exceeds 99.5% by weight, the final injection molded product has a strong transparency and becomes cloudy glass-like. On the other hand, if the content of polyester resin is less than 60% by weight, the desired surface gloss is difficult to obtain, such as a deep and elegant luster that does not develop and the appearance resembles unglazed pottery. Prolonged exposure to alcohol, fragrances, etc. is not preferable because cracks tend to occur and the strength decreases significantly. In the present invention, any suitable method can be used to mix at least one of a polyolefin resin and a methacrylic resin with the polyester resin, but the resin powders and pellets of each of the above resins are mixed in a mixer and then pelletized using a melt extruder. The method is preferred. At this time, a mixing zone may be provided at the screw tip of the extruder to enhance the kneading effect, or, for example, L/D may be 20 or more and the compression ratio may be 2.0.
It is preferable to use the above-mentioned screw or a biaxial screw because a good appearance can be obtained. Next, the injection molded product of the present invention is molded from the above-mentioned specific resin composition using an injection mold whose inner surface is satin finished, and the inner surface of the mold used at that time has the desired appearance. Depending on the pattern, part or all of the surface of the mold product may be satin finished. The satin finish on the inside of these molds is a corrosion process.
This can be done by electrical discharge machining or the like. The surface roughness of the satin pattern on the inner surface of the mold can be selected depending on the appearance of the desired molded product, but specific examples include Miyamori Metal Seisakusho's textured sample numbers: B39D, B39CD, B39C, B39BC, B39B,
B39AB, B684, B9A, etc. are preferable, but are not limited thereto. In carrying out the present invention, any commonly used injection molding machine may be used, but the degree of surface gloss of the molded product tends to be affected by the screw shape and injection molding conditions. Therefore, the screw has a compression zone and a metering zone of at least 3 pitches each, and a compression ratio of 1.5 to 3.
4 is preferred. Also important in injection molding conditions are injection speed and mold temperature. This is preferable because as the injection speed increases, a deeper surface gloss can be obtained. However, if the injection speed is excessively increased, the surface gloss around the gate will disappear, dirt will occur, and a strong flow pattern will appear, resulting in a loss of elegance, so a moderate injection speed is required. On the other hand, it is preferable that the mold temperature is set at 50℃ or less. If the temperature is higher than this, it will take a long time to cool and solidify the injection molded product, resulting in a longer molding cycle, and molding in such conditions This is not preferable because crystallization occurs in the molded product, and the deep satin aluminum-like surface gloss that has been subjected to the anodic coating treatment, which is the object of the present invention, cannot be obtained. The injection molded product of the present invention is made by injection molding a resin composition composed of a specific amount of resin as described above, so that the surface of the molded product has a pearl-like surface gloss and a satin pattern is formed on the inner surface of the mold. This is obtained for the first time by the synergistic effect of applying this to the surface of the molded product during injection molding, and the presence of a resin layer that gives a pearl-like surface gloss under the matte surface of the molded product surface is the characteristic of the present invention. It is thought that this gives a matte aluminum-like surface gloss appearance. In the present invention, additives such as dyes and pigments, ultraviolet absorbers, antistatic agents, and nucleating agents may be added without departing from the purpose of the present invention. The injection molded product of the present invention has a beautiful deep surface gloss similar to that of satin aluminum that has been subjected to the anodic coating treatment as described above, and is free from alcohol, fragrance, and other materials.
It has excellent chemical resistance to weak acids, etc., mechanical strength such as impact strength and bending strength, fragrance retention, and hygienic properties, so it is used as caps for containers for cosmetics and pharmaceuticals.
It can be preferably used for compacts, lipstick containers, fountain pen shafts, knobs of electrical appliances, etc. The present invention will be specifically explained below using Examples. Examples 1 to 5, Comparative Examples 1 to 2 [η] (dl Pellets of methacrylic copolymer having a composition of methyl methacrylate/methyl acrylate = 90/10 (weight ratio) with a ratio of 0.6 (g) to 85°C.
After drying for 20 hours at L/D = 24, supply zone 11D,
Compression zone 6D, metaling zone 7D, pitch
1D, supplied to a Toshiba Machine 40mmφ extruder equipped with a screw with a compression ratio of 2.5, and extruded to an average size of 3φ×
Pellets with dimensions of 3 mm were obtained. At this time, the cylinder temperature is 260℃ in the rear, 270℃ in the middle, and 280℃ in the front.
℃, die 280℃, and screw rotation speed 60 rpm. The measured value of [η] of polyethylene terephthalate in the obtained pellets was in the range of 0.83 to 0.87. Based on these pellets 10
Blue masterbatches with double concentration were shaped respectively, 10 parts by weight of these masterbatches and 90 parts by weight of the above-mentioned mixed resin composition pellets were mixed, vacuum dried at 150°C for 5 hours, L/D = 17, supply zone
8.5D, compression zone 5.3D, metalling zone
The inner surface is textured by Miyamori Metal Manufacturing Co., Ltd. using a Meiki Seisakusho SJ-40C injection molding machine equipped with a screw of 3.2D, pitch 0.9D, and compression ratio 3.0.
A B39C satin-finished side gate that can be molded in two pieces at the same time using a cold runner mold, weighing 15g, half of the flat plate having a wall thickness of 3mm, and the other half having a thickness of 1.5mm, and one side with a stepped matte finish. manufactured
A flat plate of 50 x 100 mm was molded. The molding conditions were as follows. Cylinder temperature is C 1 270℃, C 2 280
℃, C 3 290℃, nozzle 290℃, primary injection pressure (gauge pressure) 30Kg/cm 2 , secondary injection pressure (gauge pressure) 20Kg/cm 2
cm 2 , injection speed 50 g/sec, molding cycle 30 seconds,
The mold temperature was 10°C. The obtained molded product was evaluated for its surface appearance and changes in appearance by an ethanol immersion test at 40°C for one month. These results are shown in Table 1 along with [η] of PET in each plate. The display of appearance evaluation in Table 1 is as follows (these display methods are common to the following Examples and Comparative Examples). ◎: Those with surface gloss equivalent to the surface gloss of satin-finished aluminum that has been subjected to anodic coating treatment 〇: Those that have surface gloss that is quite close to the surface gloss of satin-finished aluminum that has been subjected to anodized coating treatment △: Those that have surface gloss that is quite similar to the surface gloss of satin-finished aluminum that has been subjected to anodic coating treatment A surface gloss that is quite similar to the surface gloss of the applied satin aluminum is observed, but its condition is weak.

【表】 実施例6〜8、比較例3〜4 第2表に示す種々の〔η〕を有する水分率
50ppm以下のPETのペレツト90重量部と70℃で
20時間真空乾燥されたエチレン−エチルアクリレ
ート共重合体10重量部とを混合したものを実施例
1で用いた押出機を用い同じ成形条件で成形し混
合樹脂ペレツトを得た。次にこれら混合樹脂ペレ
ツトを実施例1で使用した射出成形機及び金型に
より同一成形条件で射出成形を行ない実施例1で
得た平板と同じサイズの梨地加工された未着色の
平板を得た。 得られた成形品の表面外観及び40℃1ケ月エタ
ノール浸漬テストによる外観変化とについての評
価結果を第2表に示す。
[Table] Examples 6 to 8, Comparative Examples 3 to 4 Moisture content with various [η] shown in Table 2
At 70℃ with 90 parts by weight of PET pellets below 50ppm
A mixture of 10 parts by weight of ethylene-ethyl acrylate copolymer that had been vacuum-dried for 20 hours was molded using the extruder used in Example 1 under the same molding conditions to obtain mixed resin pellets. Next, these mixed resin pellets were injection molded using the injection molding machine and mold used in Example 1 under the same molding conditions to obtain a satin-finished, uncolored flat plate of the same size as the flat plate obtained in Example 1. . Table 2 shows the evaluation results for the surface appearance of the obtained molded product and the change in appearance after a one month ethanol immersion test at 40°C.

【表】【table】

Claims (1)

【特許請求の範囲】[Claims] 1 固有粘度が0.6以上のポリエステル系樹脂60
〜99.5重量%とポリオレフイン系樹脂及びメタク
リル系樹脂とからなる群から選ばれた少なくとも
一種40〜0.5重量%とからなる樹脂組成物から構
成され、金型内面が梨地加工された射出成形金型
により成形されたポリエステル製射出成形品。
1 Polyester resin 60 with an intrinsic viscosity of 0.6 or more
-99.5% by weight and at least 40% to 0.5% by weight of at least one type selected from the group consisting of polyolefin resins and methacrylic resins, using an injection molding mold with a matte finish on the inner surface of the mold. Molded polyester injection molded product.
JP13965780A 1980-10-06 1980-10-06 Molded article of polyester by injection Granted JPS5763353A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13965780A JPS5763353A (en) 1980-10-06 1980-10-06 Molded article of polyester by injection

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13965780A JPS5763353A (en) 1980-10-06 1980-10-06 Molded article of polyester by injection

Publications (2)

Publication Number Publication Date
JPS5763353A JPS5763353A (en) 1982-04-16
JPS6257487B2 true JPS6257487B2 (en) 1987-12-01

Family

ID=15250366

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13965780A Granted JPS5763353A (en) 1980-10-06 1980-10-06 Molded article of polyester by injection

Country Status (1)

Country Link
JP (1) JPS5763353A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0684462B2 (en) * 1987-09-10 1994-10-26 東レ株式会社 Resin composition for molded articles having a textured surface

Also Published As

Publication number Publication date
JPS5763353A (en) 1982-04-16

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